Ultrathin fluid-absorbent article

ABSTRACT

An absorbent core and an absorbent article respectively with improved properties, especially rewet performance, are disclosed. The absorbent core has at least two layers, wherein each layer comprising from 0 to 10% by weight fibrous material and from 90 to 100% by weight water-absorbent polymer particles, based on the sum of water-absorbent polymer particles and fibrous material. The surface-postcrosslinked water absorbent polymer particles within the upper layer have a sphericity of at least 0.89 and a CRC of at least 34 g/g. Preferably the water-absorbent polymer particles have a sphericity of at least 0.89 and the sum of the CRC and AUL (0.3 psi, 21 g cm −2 ) (EDANA 442.2-02) of the water absorbent polymer particles is at least 65 g/g.

The present invention relates to an absorbent core and an absorbent article respectively with improved properties, especially rewet performance. The absorbent core comprises at least two layers (91) (92), wherein each layer comprising from 0 to 10% by weight fibrous material and from 90 to 100% by weight water-absorbent polymer particles, based on the sum of water-absorbent polymer particles and fibrous material. Wherein the surface-postcrosslinked water absorbent polymer particles within the upper layer (91) have a sphericity of at least 0.89 and a CRC of at least 34 g/g. Preferably the water-absorbent polymer particles have a sphericity of at least 0.89 and the sum of the CRC and AUL (0.3 psi, 21 g cm⁻²) (EDANA 442.2-02) of the water absorbent polymer particles is at least 65 g/g.

The production of fluid-absorbent articles is described in the monograph “Modern Superabsorbent Polymer Technology”, F. L. Buchholz and A. T. Graham, Wiley-VCH, 1998, pages 252 to 258.

The currently commercially available disposable diapers consist typically of a liquid-pervious topsheet (A)(89), a liquid-impervious backsheet (B)(83), a water-absorbing storage layer (absorbent core) (C)(80) between layers (A) and (B), and an acquisition distribution layer (D) between layers (A) and (C).

Usually the several layers of fluid-absorbent articles fulfill definite functions such as dryness for the upper liquid-pervious layer, vapor permeability without wetting through for the lower liquid-impervious layer, a flexible, vapor permeable and fluid-absorbent core, showing fast absorption rates and being able to retain quantities of body fluids.

The preparation of water-absorbing polymer particles is likewise described in the monograph “Modern Superabsorbent Polymer Technology”, F. L. Buchholz and A. T. Graham, Wiley-VCH, 1998, pages 71 to 103. The water-absorbing polymer particles are also referred to as “fluid-absorbing polymer particles”, “superabsorbent polymers” or “superabsorbents”.

The preparation of water-absorbent polymer particles by polymerizing droplets of a monomer solution is described, for example, in EP 0 348 180 A1, WO 96/40427 A1, U.S. Pat. No. 5,269,980, WO 2008/009580 A1, WO 2008/052971 A1, WO2011/026876 A1, WO 2011/117263 A1 and WO 2014/079694.

In the last years, there has been a trend toward very thin disposable diapers. To produce thin disposable diapers, the proportion of cellulose fibers in the water-absorbing storage layer has been lowered or is almost missing.

A core-structure for ultrathin fluid-absorbent products can be formed from absorbent paper. Such structures are for example described in WO2011/086842, EP 2 565 031 A1, EP 2 668 936 A1.

But the known ultrathin fluid-absorbent products comprising absorbent paper structures have deficiencies in respect to fluid acquisition, leakage, storage and rewet properties.

It is therefore an object of the present invention to provide fluid-absorbent products with improved core performance.

It is also an object of the present invention to provide absorbent cores and absorbent articles respectively with improved fluid storage capacity to avoid leakage.

It is furthermore an object of the present invention to provide absorbent cores and absorbent articles respectively with improved rewet performance.

It is also an object of the present invention to provide absorbent cores and absorbent articles respectively with improved core structures.

The object is achieved by an absorbent core (80),

comprising at least two layers, an upper layer (91) and a lower layer (92), each layer comprising from 0 to 10% by weight fibrous material and from 90 to 100% by weight water-absorbent polymer particles, based on the sum of water-absorbent polymer particles and fibrous material; wherein the water absorbent polymer particles within the upper layer have a sphericity of at least 0.89 and a CRC of at least 34 g/g.

The object is also achieved by an absorbent core (80),

comprising at least two layers, an upper layer (91) and a lower layer (92), each layer comprising from 0 to 10% by weight fibrous material and from 90 to 100% by weight water-absorbent polymer particles, based on the sum of water-absorbent polymer particles and fibrous material; wherein the surface-postcrosslinked water absorbent polymer particles within the upper layer (91) have a sphericity of at least 0.89 and the sum of CRC and AUL (21 g cm⁻², EDANA 442.2-02) of the water absorbent polymer particles is at least 65 g/g.

The object is furthermore achieved by a fluid-absorbent core (80), comprising an upper tissue layer (95), an upper layer of surface-postcrosslinked water-absorbent polymer particles (91), a lower layer of water-absorbent polymer particles (92), at least one layer of nonwoven material (94) sandwiched between the upper layer of water-absorbent polymer particles (91) and the lower layer of water-absorbent polymer particles (92) and a lower tissue layer (96), wherein the water absorbent polymer particles within the upper layer (91) have a sphericity of at least 0.89 and the sum of CRC and AUL (21 g cm⁻², EDANA 442.2-02) of the water absorbent polymer particles is at least 65 g/g.

It is preferred that the layers are connected by adhesives, ultrasonic bonding and/or heat bonding.

The object is also achieved by a fluid-absorbent article, comprising

(A) an upper liquid-pervious sheet (89), (B) a lower liquid-impervious sheet (83), and (C) a fluid-absorbent core (80) between the upper sheet (89) and the lower sheet (83) comprising at least two layers, an upper layer (91) and a lower layer (92), each layer comprising from 0 to 10% by weight fibrous material and from 90 to 100% by weight water-absorbent polymer particles, based on the sum of water-absorbent polymer particles and fibrous material; (D) an optional acquisition-distribution layer (D) between (89) and (80), (E) other optional components, wherein the water absorbent polymer particles within the upper layer (91) have a sphericity of at least 0.89 and the sum of the CRC and AUL (21 g cm⁻², EDANA 442.2-02) of the water absorbent polymer particles is at least 65 g/g.

The object is furthermore achieved by a fluid-absorbent article, comprising

a fluid absorbent core (80) between the upper liquid-pervious sheet (89) and the lower liquid-impervious sheet (83), comprising an upper tissue layer (95), an upper layer of water-absorbent polymer particles (91), a lower layer of water-absorbent polymer particles (92), at least one layer of nonwoven material (94) sandwiched between the upper layer of water-absorbent polymer particles (91) and the lower layer of water-absorbent polymer particles (92) and a lower tissue layer (96). It is preferred that the layers are connected by adhesives, ultrasonic bonding and/or heat bonding.

Furthermore according to another embodiment of the invention each layer of water-absorbent polymer particles of the absorbent core contains at least 100 gsm water absorbent polymer particles.

The fluid-absorbent structures of the present invention show improved liquid acquisition and retention behavior.

BRIEF DESCRIPTION OF THE DRAWINGS

FIGS. 1 to 15 illustrate preferred embodiments for the dropletization process:

FIG. 1 is an illustration of the process scheme.

FIG. 2 is an illustration of the process scheme using dry air.

FIG. 3 is an illustration of an arrangement of the T_outlet measurement.

FIG. 4 is an illustration of an arrangement of dropletizer units with 3 droplet plates.

FIG. 5 is an illustration of an arrangement of dropletizer units with 9 droplet plates.

FIG. 6 is an illustration of an arrangement of dropletizer units with 9 droplet plates.

FIG. 7 is a schematic view of a longitudinal cut of a dropletizer unit.

FIG. 8 is a cross sectional view of a dropletizer unit.

FIG. 9 is a top-view of a bottom of the internal fluidized bed.

FIG. 10 is a schematic view of openings in the bottom of the internal fluidized bed.

FIG. 11 is a top view of a rake stirrer for the intern fluidized bed.

FIG. 12 is a cross sectional view of a rake stirrer for the intern fluidized bed.

FIG. 13 is an illustration of a process scheme for surface-postcrosslinking.

FIG. 14 is an illustration of a process scheme for surface-postcrosslinking and coating.

FIG. 15 is an illustration of a contact dryer for surface-postcrosslinking.

FIG. 16 is a schematic view of a fluid-absorbent article.

FIG. 17 is a schematic view of an absorbent core.

FIG. 18 is an illustration of a possible production process for an absorbent core.

According to the invention especially the at least two layered cores/absorbent papers, contain at least in the upper layer (91) water-absorbent polymer particles with a sphericity of at least 0.89.

Suitable water-absorbent polymers are produced by a process, comprising the steps forming water-absorbent polymer particles by polymerizing a monomer solution, comprising

-   a) at least one ethylenically unsaturated monomer which bears acid     groups and may be at least partly neutralized, -   b) optionally one or more crosslinker, -   c) at least one initiator, -   d) optionally one or more ethylenically unsaturated monomers     copolymerizable with the monomers mentioned under a), -   e) optionally one or more water-soluble polymers, and -   f) water,     coating of water-absorbent polymer particles with at least one     surface-postcrosslinker and thermal surface-postcrosslinking of the     coated water-absorbent polymer particles.

It is preferred to produce the water-absorbent polymer particles polymerizing droplets of the monomer in a surrounding heated gas phase, for example using a system described in WO 2008/040715 A2, WO 2008/052971 A1, WO 2008/069639 A1 and WO 2008/086976 A1, WO 2014/079694, WO 2015/028327, WO 2015/028158.

DETAILED DESCRIPTION OF THE INVENTION A. Definitions

As used herein, the term “fluid-absorbent article” refers to any three-dimensional solid material being able to acquire and store fluids discharged from the body. Preferred fluid-absorbent articles are disposable fluid-absorbent articles that are designed to be worn in contact with the body of a user such as disposable fluid-absorbent pantyliners, sanitary napkins, catamenials, incontinence inserts/pads, diapers, training pant diapers, breast pads, interlabial inserts/pads or other articles useful for absorbing body fluids.

As used herein, the term “fluid-absorbent composition” refers to a component of the fluid-absorbent article which is primarily responsible for the fluid handling of the fluid-absorbent article including acquisition, transport, distribution and storage of body fluids.

As used herein, the term “fluid-absorbent core”, “absorbent core” or “absorbent paper” refers to a fluid-absorbent composition comprising at least two layers of water-absorbent polymer particles and optionally fibrous material, nonwoven material, tissue material and optionally adhesive. The fluid-absorbent core is primarily responsible for the fluid handling/management of the fluid-absorbent article including acquisition, transport, distribution, storage and retention of body fluids.

As used herein, the term “layer” refers to a fluid-absorbent composition whose primary dimension is along its length and width.

As used herein the term “x-dimension” refers to the length, and the term “y-dimension” refers to the width of the fluid-absorbent composition, layer, core or article. Generally, the term “x-y-dimension” refers to the plane, orthogonal to the height or thickness of the fluid-absorbent composition, layer, core or article.

As used herein the term “z-dimension” refers to the dimension orthogonal to the length and width of the fluid absorbent composition, layer, core or article. Generally, the term “z-dimension” refers to the height of the fluid-absorbent composition, layer, core or article.

As used herein, the term “basis weight” indicates the weight of the fluid-absorbent core per square meter and it includes the chassis of the fluid-absorbent article. The basis weight is determined at discrete regions of the fluid-absorbent core: the front overall average is the basis weight of the fluid-absorbent core 5.5 cm forward of the center of the core to the front distal edge of the core; the insult zone is the basis weight of the fluid-absorbent core 5.5 cm forward and 0.5 cm backwards of the center of the core; the back overall average is the basis weight of the fluid-absorbent core 0.5 cm backward of the center of the core to the rear distal edge of the core.

Further, it should be understood, that the term “upper” refers to fluid-absorbent composition which are nearer to the wearer of the fluid-absorbent article. Generally, the topsheet is the nearest composition to the wearer of the fluid-absorbent article, hereinafter described as “upper liquid-pervious layer”. Contrarily, the term “lower” refers to fluid-absorbent compositions which are away from the wearer of the fluid-absorbent article. Generally, the backsheet is the component which is furthermost away from the wearer of the fluid-absorbent article, hereinafter described as “lower liquid-impervious layer”.

As used herein, the term “liquid-pervious” refers to a substrate, layer or a laminate thus permitting liquids, i.e. body fluids such as urine, menses and/or vaginal fluids to readily penetrate through its thickness.

As used herein, the term “liquid-impervious” refers to a substrate, layer or a laminate that does not allow body fluids to pass through in a direction generally perpendicular to the plane of the layer at the point of liquid contact under ordinary use conditions.

As used herein, the term “chassis” refers to fluid-absorbent material comprising the upper liquid-pervious layer and the lower liquid-impervious layer, elastication and closure systems for the absorbent article.

As used herein, the term “hydrophilic” refers to the wettability of fibers by water deposited on these fibers. The term “hydrophilic” is defined by the contact angle and surface tension of the body fluids. According to the definition of Robert F. Gould in the 1964 American Chemical Society publication “Contact angle, wettability and adhesion”, a fiber is referred to as hydrophilic, when the contact angle between the liquid and the fiber, especially the fiber surface, is less than 90° or when the liquid tends to spread spontaneously on the same surface.

Contrarily, term “hydrophobic” refers to fibers showing a contact angle of greater than 90° or no spontaneously spreading of the liquid across the surface of the fiber.

As used herein, the term “body fluids” refers to any fluid produced and discharged by human or animal body, such as urine, menstrual fluids, faeces, vaginal secretions and the like.

As used herein, the term “breathable” refers to a substrate, layer, film or a laminate that allows vapour to escape from the fluid-absorbent article, while still preventing fluids from leakage. Breathable substrates, layers, films or laminates may be porous polymeric films, nonwoven laminates from spunbond and melt-blown layers, laminates from porous polymeric films and nonwovens.

As used herein, the term “longitudinal” refers to a direction running perpendicular from a waist edge to an opposing waist edge of the fluid-absorbent article.

B. Water-Absorbent Polymer Particles

The water-absorbent polymer particles are prepared by a process, comprising the steps forming water-absorbent polymer particles by polymerizing a monomer solution, comprising

-   g) at least one ethylenically unsaturated monomer which bears acid     groups and may be at least partly neutralized, -   h) optionally one or more crosslinker, -   i) at least one initiator, -   j) optionally one or more ethylenically unsaturated monomers     copolymerizable with the monomers mentioned under a), -   k) optionally one or more water-soluble polymers, and -   l) water,     coating of water-absorbent polymer particles with at least one     surface-postcrosslinker and thermal surface-postcrosslinking of the     coated water-absorbent polymer particles.

Preferably the content of residual monomers in the water-absorbent polymer particles prior to coating with a surface-postcrosslinker is in the range from 0.03 to 15% by weight, a preferred surface-postcrosslinker is an alkylene carbonate, and the temperature during the thermal surface-postcrosslinking is in the range from 100 to 180° C.

The water-absorbent polymer particles are typically insoluble but swellable in water.

The monomers a) are preferably water-soluble, i.e. the solubility in water at 23° C. is typically at least 1 g/100 g of water, preferably at least 5 g/100 g of water, more preferably at least 25 g/100 g of water, most preferably at least 35 g/100 g of water.

Suitable monomers a) are, for example, ethylenically unsaturated carboxylic acids such as acrylic acid, methacrylic acid, maleic acid, and itaconic acid. Particularly preferred monomers are acrylic acid and methacrylic acid. Very particular preference is given to acrylic acid.

Further suitable monomers a) are, for example, ethylenically unsaturated sulfonic acids such as vinylsulfonic acid, styrenesulfonic acid and 2-acrylamido-2-methylpropanesulfonic acid (AMPS).

Impurities may have a strong impact on the polymerization. Preference is given to especially purified monomers a). Useful purification methods are disclosed in WO 2002/055469 A1, WO 2003/078378 A1 and WO 2004/035514 A1. A suitable monomer a) is according to WO 2004/035514 A1 purified acrylic acid having 99.8460% by weight of acrylic acid, 0.0950% by weight of acetic acid, 0.0332% by weight of water, 0.0203 by weight of propionic acid, 0.0001% by weight of furfurals, 0.0001% by weight of maleic anhydride, 0.0003% by weight of diacrylic acid and 0.0050% by weight of hydroquinone monomethyl ether.

Polymerized diacrylic acid is a source for residual monomers due to thermal decomposition. If the temperatures during the process are low, the concentration of diacrylic acid is no more critical and acrylic acids having higher concentrations of diacrylic acid, i.e. 500 to 10,000 ppm, can be used for the inventive process.

The content of acrylic acid and/or salts thereof in the total amount of monomers a) is preferably at least 50 mol %, more preferably at least 90 mol %, most preferably at least 95 mol %.

The acid groups of the monomers a) are typically partly neutralized in the range of 0 to 100 mol %, preferably to an extent of from 25 to 85 mol %, preferentially to an extent of from 50 to 80 mol %, more preferably from 60 to 75 mol %, for which the customary neutralizing agents can be used, preferably alkali metal hydroxides, alkali metal oxides, alkali metal carbonates or alkali metal hydrogen carbonates, and mixtures thereof. Instead of alkali metal salts, it is also possible to use ammonia or organic amines, for example, triethanolamine. It is also possible to use oxides, carbonates, hydrogencarbonates and hydroxides of magnesium, calcium, strontium, zinc or aluminum as powders, slurries or solutions and mixtures of any of the above neutralization agents. Example for a mixture is a solution of sodiumaluminate. Sodium and potassium are particularly preferred as alkali metals, but very particular preference is given to sodium hydroxide, sodium carbonate or sodium hydrogen carbonate, and mixtures thereof. Typically, the neutralization is achieved by mixing in the neutralizing agent as an aqueous solution, as a melt or preferably also as a solid. For example, sodium hydroxide with water content significantly below 50% by weight may be present as a waxy material having a melting point above 23° C. In this case, metered addition as piece material or melt at elevated temperature is possible.

Optionally, it is possible to add to the monomer solution, or to starting materials thereof, one or more chelating agents for masking metal ions, for example iron, for the purpose of stabilization. Suitable chelating agents are, for example, alkali metal citrates, citric acid, alkali metal tartrates, alkali metal lactates and glycolates, pentasodium triphosphate, ethylenediamine tetraacetate, nitrilotriacetic acid, and all chelating agents known under the Trilon® name, for example Trilon® C (pentasodium diethylenetriaminepentaacetate), Trilon® D (trisodium (hydroxyethyl)-ethylenediaminetriacetate), Trilon® M (methylglycinediacetic acid) and Cublen®.

The monomers a) comprise typically polymerization inhibitors, preferably hydroquinone monoethers, as inhibitor for storage.

The monomer solution comprises preferably up to 250 ppm by weight, more preferably not more than 130 ppm by weight, most preferably not more than 70 ppm by weight, preferably not less than 10 ppm by weight, more preferably not less than 30 ppm by weight and especially about 50 ppm by weight of hydroquinone monoether, based in each case on acrylic acid, with acrylic acid salts being counted as acrylic acid. For example, the monomer solution can be prepared using acrylic acid having appropriate hydroquinone monoether content. The hydroquinone monoethers may, however, also be removed from the monomer solution by absorption, for example on activated carbon.

Preferred hydroquinone monoethers are hydroquinone monomethyl ether (MEHQ) and/or alpha-tocopherol (vitamin E).

Suitable crosslinkers b) are compounds having at least two groups suitable for crosslinking. Such groups are, for example, ethylenically unsaturated groups which can be polymerized by a free-radical mechanism into the polymer chain and functional groups which can form covalent bonds with the acid groups of monomer a). In addition, polyvalent metal ions which can form coordinate bond with at least two acid groups of monomer a) are also suitable crosslinkers b).

The crosslinkers b) are preferably compounds having at least two free-radically polymerizable groups which can be polymerized by a free-radical mechanism into the polymer network. Suitable crosslinkers b) are, for example, ethylene glycol dimethacrylate, diethylene glycol diacrylate, polyethylene glycol diacrylate, allyl methacrylate, trimethylolpropane triacrylate, triallylamine, tetraallylammonium chloride, tetraallyloxyethane, as described in EP 0 530 438 A1, di- and triacrylates, as described in EP 0 547 847 A1, EP 0 559 476 A1, EP 0 632 068 A1, WO 93/21237 A1, WO 2003/104299 A1, WO 2003/104300 A1, WO 2003/104301 A1 and in DE 103 31 450 A1, mixed acrylates which, as well as acrylate groups, comprise further ethylenically unsaturated groups, as described in DE 103 314 56 A1 and DE 103 55 401 A1, or crosslinker mixtures, as described, for example, in DE 195 43 368 A1, DE 196 46 484 A1, WO 90/15830 A1 and WO 2002/32962 A2.

Suitable crosslinkers b) are in particular pentaerythritol triallyl ether, tetraallyloxyethane, polyethyleneglycole diallylethers (based on polyethylene glycole having a molecular weight between 400 and 20000 g/mol), N,N′-methylenebisacrylamide, 15-tuply ethoxylated trimethylolpropane, polyethylene glycol diacrylate, trimethylolpropane triacrylate and triallylamine.

Very particularly preferred crosslinkers b) are the polyethoxylated and/or -propoxylated glycerols which have been esterified with acrylic acid or methacrylic acid to give di- or triacrylates, as described, for example in WO 2003/104301 A1. Di- and/or triacrylates of 3- to 18-tuply ethoxylated glycerol are particularly advantageous. Very particular preference is given to di- or triacrylates of 1- to 5-tuply ethoxylated and/or propoxylated glycerol. Most preferred are the triacrylates of 3- to 5-tuply ethoxylated and/or propoxylated glycerol and especially the triacrylate of 3-tuply ethoxylated glycerol.

The amount of crosslinker b) is preferably from 0.0001 to 0.6% by weight, more preferably from 0.001 to 0.2% by weight, most preferably from 0.01 to 0.06% by weight, based in each case on monomer a). On increasing the amount of crosslinker b) the centrifuge retention capacity (CRC) decreases and the absorption under a pressure of 21.0 g/cm² (AUL) passes through a maximum.

The surface-postcrosslinked polymer particles of the present invention surprisingly require very little or even no cross-linker during the polymerization step. So, in one particularly preferred embodiment of the present invention no crosslinker b) is used.

The initiators c) used may be all compounds which disintegrate into free radicals under the polymerization conditions, for example peroxides, hydroperoxides, hydrogen peroxide, persulfates, azo compounds and redox initiators. Preference is given to the use of water-soluble initiators. In some cases, it is advantageous to use mixtures of various initiators, for example mixtures of hydrogen peroxide and sodium or potassium peroxodisulfate. Mixtures of hydrogen peroxide and sodium peroxodisulfate can be used in any proportion.

Particularly preferred initiators c) are azo initiators such as 2,2′-azobis[2-(2-imidazolin-2-yl)propane] dihydrochloride and 2,2′-azobis[2-(5-methyl-2-imidazolin-2-yl)propane] dihydrochloride, 2,2′-azobis(2-amidinopropane) dihydrochloride, 4,4′-azobis(4-cyanopentanoic acid), 4,4′-azobis(4-cyanopentanoic acid) sodium salt, 2,2′-azobis[2-methyl-N-(2-hydroxyethyl)propionamide], and photoinitiators such as 2-hydroxy-2-methylpropiophenone and 1-[4-(2-hydroxyethoxy)phenyl]-2-hydroxy-2-methyl-1-propan-1-one, redox initiators such as sodium persulfate/hydroxymethylsulfinic acid, ammonium peroxodisulfate/hydroxymethylsulfinic acid, hydrogen peroxide/hydroxymethylsulfinic acid, sodium persulfate/ascorbic acid, ammonium peroxodisulfate/ascorbic acid and hydrogen peroxide/ascorbic acid, photoinitiators such as 1-[4-(2-hydroxyethoxy)phenyl]-2-hydroxy-2-methyl-1-propan-1-one, and mixtures thereof. The reducing component used is, however, preferably a mixture of the sodium salt of 2-hydroxy-2-sulfinatoacetic acid, the disodium salt of 2-hydroxy-2-sulfonatoacetic acid and sodium bisulfite. Such mixtures are obtainable as Brüggolite® FF6 and Brüggolite® FF7 (Brüggemann Chemicals; Heilbronn; Germany). Of course it is also possible within the scope of the present invention to use the purified salts or acids of 2-hydroxy-2-sulfinatoacetic acid and 2-hydroxy-2-sulfonatoacetic acid—the latter being available as sodium salt under the trade name Blancolene® (Brüggemann Chemicals; Heilbronn; Germany).

The initiators are used in customary amounts, for example in amounts of from 0.001 to 5% by weight, preferably from 0.01 to 2% by weight, most preferably from 0.05 to 0.5% by weight, based on the monomers a).

Examples of ethylenically unsaturated monomers d) which are copolymerizable with the monomers a) are acrylamide, methacrylamide, hydroxyethyl acrylate, hydroxyethyl methacrylate, dimethylaminoethyl acrylate, dimethylaminoethyl methacrylate, dimethylaminopropyl acrylate and diethylaminopropyl methacrylate.

Useful water-soluble polymers e) include polyvinyl alcohol, modified polyvinyl alcohol comprising acidic side groups for example Poval® K (Kuraray Europe GmbH; Frankfurt; Germany), polyvinylpyrrolidone, starch, starch derivatives, modified cellulose such as methylcellulose, carboxymethylcellulose or hydroxyethylcellulose, gelatin, polyglycols or polyacrylic acids, polyesters and polyamides, polylactic acid, polyglycolic acid, co-polylactic-polyglycolic acid, polyvinylamine, polyallylamine, water soluble copolymers of acrylic acid and maleic acid available as Sokalan® (BASF SE; Ludwigshafen; Germany), preferably starch, starch derivatives and modified cellulose.

For optimal action, the preferred polymerization inhibitors require dissolved oxygen. Therefore, the monomer solution can be freed of dissolved oxygen before the polymerization by inertization, i.e. flowing through with an inert gas, preferably nitrogen. It is also possible to reduce the concentration of dissolved oxygen by adding a reducing agent. The oxygen content of the monomer solution is preferably lowered before the polymerization to less than 1 ppm by weight, more preferably to less than 0.5 ppm by weight.

The water content of the monomer solution is preferably less than 65% by weight, preferentially less than 62% by weight, more preferably less than 60% by weight, most preferably less than 58% by weight.

The monomer solution has, at 20° C., a dynamic viscosity of preferably from 0.002 to 0.02 Pa·s, more preferably from 0.004 to 0.015 Pa·s, most preferably from 0.005 to 0.01 Pa·s. The mean droplet diameter in the droplet generation rises with rising dynamic viscosity.

The monomer solution has, at 20° C., a density of preferably from 1 to 1.3 g/cm³, more preferably from 1.05 to 1.25 g/cm³, most preferably from 1.1 to 1.2 g/cm³.

The monomer solution has, at 20° C., a surface tension of from 0.02 to 0.06 N/m, more preferably from 0.03 to 0.05 N/m, most preferably from 0.035 to 0.045 N/m. The mean droplet diameter in the droplet generation rises with rising surface tension.

Polymerization

The monomer solution is polymerized.

It is preferred to produce the water-absorbent polymer particles polymerizing droplets of the monomer in a surrounding heated gas phase, for example using a system described in WO 2008/040715 A2, WO 2008/052971 A1, WO 2008/069639 A1 and WO 2008/086976 A1, WO 2014/079694, WO 2015/028327, WO 2015/028158.

Especially at least the upper layer (91) of the inventive absorbent core (80) or the inventive fluid-absorbent article respectively comprises water-absorbent polymer particles produced by polymerizing droplets of the monomer in a surrounding heated gas phase.

The droplets are preferably generated by means of a droplet plate. A droplet plate is a plate having a multitude of bores, the liquid entering the bores from the top. The droplet plate or the liquid can be oscillated, which generates a chain of ideally monodisperse droplets at each bore on the underside of the droplet plate. In a preferred embodiment, the droplet plate is not agitated.

Within the scope of the present invention it is also possible to use two or more droplet plates with different bore diameters so that a range of desired particle sizes can be produced. It is preferable that each droplet plate carries only one bore diameter, however mixed bore diameters in one plate are also possible.

The number and size of the bores are selected according to the desired capacity and droplet size. The droplet diameter is typically 1.9 times the diameter of the bore. What is important here is that the liquid to be dropletized does not pass through the bore too rapidly and the pressure drop over the bore is not too great. Otherwise, the liquid is not dropletized, but rather the liquid jet is broken up (sprayed) owing to the high kinetic energy. In a preferred embodiment of the present invention the pressure drop is from 4 to 5 bar. The Reynolds number based on the throughput per bore and the bore diameter is preferably less than 2000, preferentially less than 1600, more preferably less than 1400 and most preferably less than 1200.

The underside of the droplet plate has at least in part a contact angle preferably of at least 60°, more preferably at least 75° and most preferably at least 90° with regard to water. The contact angle is a measure of the wetting behavior of a liquid, in particular water, with regard to a surface, and can be determined using conventional methods, for example in accordance with ASTM D 5725. A low contact angle denotes good wetting, and a high contact angle denotes poor wetting.

It is also possible for the droplet plate to consist of a material having a lower contact angle with regard to water, for example a steel having the German construction material code number of 1.4571, and be coated with a material having a larger contact angle with regard to water. Useful coatings include for example fluorous polymers, such as perfluoroalkoxyethylene, polytetrafluoroethylene, ethylene-chlorotrifluoroethylene copolymers, ethylene-tetrafluoroethylene copolymers and fluorinated polyethylene.

The coatings can be applied to the substrate as a dispersion, in which case the solvent is subsequently evaporated off and the coating is heat treated. For polytetrafluoroethylene this is described for example in U.S. Pat. No. 3,243,321.

Further coating processes are to be found under the headword “Thin Films” in the electronic version of “Ullmann's Encyclopedia of Industrial Chemistry” (Updated Sixth Edition, 2000 Electronic Release).

The coatings can further be incorporated in a nickel layer in the course of a chemical nickelization. It is the poor wettability of the droplet plate that leads to the production of monodisperse droplets of narrow droplet size distribution.

The droplet plate has preferably at least 5, more preferably at least 25, most preferably at least 50 and preferably up to 2000, more preferably up to 1500 bores, most preferably up to 1000.

The diameter of the bores is adjusted to the desired droplet size.

The spacing of the bores is usually from 2 to 50 mm, preferably from 3 to 40 mm, more preferably from 4 to 30 mm, most preferably from 5 to 25 mm. Smaller spacings of the bores may cause agglomeration of the polymerizing droplets.

The diameter of the bores size area is 1900 to 22300 μm², more preferably from 7800 to 20100 μm², most preferably from 11300 to 17700 μm². Circular bores are preferred with a bore size from 50 to 170 μm, more preferably from 100 to 160 μm, most preferably from 120 to 150 μm.

For optimizing the average particle diameter, droplet plates with different bore diameters can be used. The variation can be done by different bores on one plate or by using different plates, where each plate has a different bore diameter. The average particle size distribution can be monomodal, bimodal or multimodal. Most preferably it is monomodal or bimodal.

The temperature of the monomer solution as it passes through the bore is preferably from 5 to 80° C., more preferably from 10 to 70° C., most preferably from 30 to 60° C.

A carrier gas flows through the reaction zone. The carrier gas may be conducted through the reaction zone in cocurrent to the free-falling droplets of the monomer solution, i.e. from the top downward. After one pass, the gas is preferably recycled at least partly, preferably to an extent of at least 50%, more preferably to an extent of at least 75%, into the reaction zone as cycle gas. Typically, a portion of the carrier gas is discharged after each pass, preferably up to 10%, more preferably up to 3% and most preferably up to 1%.

The oxygen content of the carrier gas is preferably from 0.1 to 25% by volume, more preferably from 1 to 10% by volume, most preferably from 2 to 7% by weight. In the scope of the present invention it is also possible to use a carrier gas which is free of oxygen. As well as oxygen, the carrier gas preferably comprises nitrogen. The nitrogen content of the gas is preferably at least 80% by volume, more preferably at least 90% by volume, most preferably at least 95% by volume. Other possible carrier gases may be selected from carbon dioxide, argon, xenon, krypton, neon, helium, sulfurhexafluoride. Any mixture of carrier gases may be used. It is also possible to use air as carrier gas. The carrier gas may also become loaded with water and/or acrylic acid vapors.

The gas velocity is preferably adjusted such that the flow in the reaction zone (5) is directed, for example no convection currents opposed to the general flow direction are present, and is preferably from 0.1 to 2.5 m/s, more preferably from 0.3 to 1.5 m/s, even more preferably from 0.5 to 1.2 m/s, most preferably from 0.7 to 0.9 m/s.

The gas entrance temperature, i.e. the temperature with which the gas enters the reaction zone, is preferably from 160 to 200° C., more preferably from 165 to 195° C., even more preferably from 170 to 190° C., most preferably from 175 to 185° C.

The steam content of the gas that enters the reaction zone is preferably from 0.01 to 0.15 kg per kg dry gas, more from 0.02 to 0.12 kg per kg dry gas, most from 0.03 to 0.10 kg per kg dry gas.

The gas entrance temperature is controlled in such a way that the gas exit temperature, i.e. the temperature with which the gas leaves the reaction zone, is less than 150° C., preferably from 90 to 140° C., more preferably from 100 to 130° C., even more preferably from 105 to 125° C., most preferably from 110 to 120° C.

The water-absorbent polymer particles can be divided into three categories: water-absorbent polymer particles of Type 1 are particles with one cavity, water-absorbent polymer particles of Type 2 are particles with more than one cavity, and water-absorbent polymer particles of Type 3 are solid particles with no visible cavity.

The morphology of the water-absorbent polymer particles can be controlled by the reaction conditions during polymerization. Water-absorbent polymer particles having a high amount of particles with one cavity (Type 1) can be prepared by using low gas velocities and high gas exit temperatures. Water-absorbent polymer particles having a high amount of particles with more than one cavity (Type 2) can be prepared by using high gas velocities and low gas exit temperatures.

Water-absorbent polymer particles having more than one cavity (Type 2) show an improved mechanical stability.

The reaction can be carried out under elevated pressure or under reduced pressure, preferably from 1 to 100 mbar below ambient pressure, more preferably from 1.5 to 50 mbar below ambient pressure, most preferably from 2 to 10 mbar below ambient pressure. The reaction off-gas, i.e. the gas leaving the reaction zone, may be cooled in a heat exchanger. This condenses water and unconverted monomer a). The reaction off-gas can then be reheated at least partly and recycled into the reaction zone as cycle gas. A portion of the reaction off-gas can be discharged and replaced by fresh gas, in which case water and unconverted monomers a) present in the reaction off-gas can be removed and recycled.

Particular preference is given to a thermally integrated system, i.e. a portion of the waste heat in the cooling of the off-gas is used to heat the cycle gas.

The reactors can be trace-heated. In this case, the trace heating is adjusted such that the wall temperature is at least 5° C. above the internal surface temperature and condensation on the surfaces is reliably prevented.

Thermal Posttreatment

The water-absorbent polymer particles obtained by dropletization may be thermal posttreated for adjusting the content of residual monomers to the desired value.

Generally the level of residual monomers can be influenced by process parameter settings, for example; the temperature of posttreatment of the water-absorbent particles. The residual monomers can be removed better at relatively high temperatures and relatively long residence times. What is important here is that the water-absorbent polymer particles are not too dry. In the case of excessively dry particles, the residual monomers decrease only insignificantly. Too high a water content increases the caking tendency of the water-absorbent polymer particles.

The thermal posttreatment can be done in a fluidized bed. In a preferred embodiment of the present invention an internal fluidized bed is used. An internal fluidized bed means that the product of the dropletization polymerization is accumulated in a fluidized bed below the reaction zone.

The residual monomers can be removed during the thermal posttreatment. What is important here is that the water-absorbent polymer particles are not too dry. In the case of excessively dry particles, the residual monomers decrease only insignificantly. A too high water content increases the caking tendency of the water-absorbent polymer particles.

In the fluidized state, the kinetic energy of the polymer particles is greater than the cohesion or adhesion potential between the polymer particles.

The fluidized state can be achieved by a fluidized bed. In this bed, there is upward flow toward the water-absorbing polymer particles, so that the particles form a fluidized bed. The height of the fluidized bed is adjusted by gas rate and gas velocity, i.e. via the pressure drop of the fluidized bed (kinetic energy of the gas).

The velocity of the gas stream in the fluidized bed is preferably from 0.3 to 2.5 m/s, more preferably from 0.4 to 2.0 m/s, most preferably from 0.5 to 1.5 m/s.

The pressure drop over the bottom of the internal fluidized bed is preferably from 1 to 100 mbar, more preferably from 3 to 50 mbar, most preferably from 5 to 25 mbar.

The moisture content of the water-absorbent polymer particles at the end of the thermal posttreatment is preferably from 1 to 20% by weight, more preferably from 2 to 15% by weight, even more preferably from 3 to 12% by weight, most preferably 5 to 8% by weight. The temperature of the water-absorbent polymer particles during the thermal posttreatment is from 20 to 140° C., preferably from 40 to 110° C., more preferably from 50 to 105° C., most preferably from 60 to 100° C.

The average residence time in the internal fluidized bed is from 10 to 300 minutes, preferably from 60 to 270 minutes, more preferably from 40 to 250 minutes, most preferably from 120 to 240 minutes.

The condition of the fluidized bed can be adjusted for reducing the amount of residual monomers of the water-absorbent polymers leaving the fluidized bed. The amount of residual monomers can be reduced to levels below 0.1% by weight by a thermal posttreatment using additional steam.

The steam content of the gas is preferably from 0.005 to 0.25 kg per kg of dry gas, more preferably from 0.01 to 0.2 kg per kg of dry gas, most preferably from 0.02 to 0.15 kg per kg of dry gas.

By using additional steam the condition of the fluidized bed can be adjusted that the amount of residual monomers of the water-absorbent polymers leaving the fluidized bed is from 0.03 to 15% by weight, preferably from 0.05 to 12% by weight, more preferably from 0.1 to 10% by weight, even more preferably from 0.15 to 7.5% by weight most preferably from 0.2 to 5% by weight, even most preferably from 0.25 to 2.5% by weight.

The level of residual monomers in the water-absorbent polymer has in important impact on the properties of the later formed surface-postcrosslinked water-absorbent polymer particles. That means that very low levels of residual monomers must be avoided.

It is preferred that the thermal posttreatment is completely or at least partially done in an external fluidized bed. The operating conditions of the external fluidized bed are within the scope for the internal fluidized bed as described above.

It is alternatively preferred that the thermal posttreatment is done in an external mixer with moving mixing tools as e.g. described in WO 2011/117215 A1, preferably horizontal mixers, such as screw mixers, disk mixers, screw belt mixers and paddle mixers. Suitable mixers are, for example, Becker shovel mixers (Gebr. Lödige Maschinenbau GmbH; Paderborn; Germany), Nara paddle mixers (NARA Machinery Europe; Frechen; Germany), Pflugschar® plowshare mixers (Gebr. Lödige Maschinenbau GmbH; Paderborn; Germany), Vrieco-Nauta Continuous Mixers (Hosokawa Micron BV; Doetinchem; the Netherlands), Processall Mixmill Mixers (Processall Incorporated; Cincinnati; U.S.A.) and Ruberg continuous flow mixers (Gebrüder Ruberg GmbH & Co KG, Nieheim, Germany). Ruberg continuous flow mixers, Becker shovel mixers and Pflugschar® plowshare mixers are preferred.

The thermal posttreatment can be done in a discontinuous external mixer or a continuous external mixer.

The amount of gas to be used in the discontinuous external mixer is preferably from 0.01 to 5 Nm³/h, more preferably from 0.05 to 2 Nm³/h, most preferably from 0.1 to 0.5 Nm³/h, based in each case on kg water-absorbent polymer particles.

The amount of gas to be used in the continuous external mixer is preferably from 0.01 to 5 Nm³/h, more preferably from 0.05 to 2 Nm³/h, most preferably from 0.1 to 0.5 Nm³/h, based in each case on kg/h throughput of water-absorbent polymer particles.

The other constituents of the gas are preferably nitrogen, carbon dioxide, argon, xenon, krypton, neon, helium, air or air/nitrogen mixtures, more preferably nitrogen or air/nitrogen mixtures comprising less than 10% by volume of oxygen. Oxygen may cause discoloration.

The morphology of the water-absorbent polymer particles can also be controlled by the reaction conditions during thermal posttreatment. Water-absorbent polymer particles having a high amount of particles with one cavity (Type 1) can be prepared by using high product temperatures and short residence times. Water-absorbent polymer particles having a high amount of particles with more than one cavity (Type 2) can be prepared by using low product temperatures and long residence times.

Surface-Postcrosslinking

The polymer particles can be surface-postcrosslinked for further improvement of the properties.

Surface-postcrosslinkers are compounds which comprise groups which can form at least two covalent bonds with the carboxylate groups of the polymer particles. Suitable compounds are, for example, polyfunctional amines, polyfunctional amidoamines, polyfunctional epoxides, as described in EP 0 083 022 A2, EP 0 543 303 A1 and EP 0 937 736 A2, di- or polyfunctional alcohols as described in DE 33 14 019 A1, DE 35 23 617 A1 and EP 0 450 922 A2, or β-hydroxyalkylamides, as described in DE 102 04 938 A1 and U.S. Pat. No. 6,239,230. Also ethyleneoxide, aziridine, glycidol, oxetane and its derivatives may be used.

Polyvinylamine, polyamidoamines and polyvinylalcohole are examples of multifunctional polymeric surface-postcrosslinkers.

In addition, DE 40 20 780 C1 describes alkylene carbonates, DE 198 07 502 A1 describes 1,3-oxazolidin-2-one and its derivatives such as 2-hydroxyethyl-1,3-oxazolidin-2-one, DE 198 07 992 C1 describes bis- and poly-1,3-oxazolidin-2-ones, EP 0 999 238 A1 describes bis- and poly-1,3-oxazolidines, DE 198 54 573 A1 describes 2-oxotetrahydro-1,3-oxazine and its derivatives, DE 198 54 574 A1 describes N-acyl-1,3-oxazolidin-2-ones, DE 102 04 937 A1 describes cyclic ureas, DE 103 34 584 A1 describes bicyclic amide acetals, EP 1 199 327 A2 describes oxetanes and cyclic ureas, and WO 2003/31482 A1 describes morpholine-2,3-dione and its derivatives, as suitable surface-postcrosslinkers.

In addition, it is also possible to use surface-postcrosslinkers which comprise additional polymerizable ethylenically unsaturated groups, as described in DE 37 13 601 A1.

The at least one surface-postcrosslinker is selected from alkylene carbonates, 1,3-oxazolidin-2-ones, bis- and poly-1,3-oxazolidin-2-ones, bis- and poly-1,3-oxazolidines, 2-oxotetrahydro-1,3-oxazines, N-acyl-1,3-oxazolidin-2-ones, cyclic ureas, bicyclic amide acetals, oxetanes, and morpholine-2,3-diones. Suitable surface-postcrosslinkers are ethylene carbonate, 3-methyl-1,3-oxazolidin-2-one, 3-methyl-3-oxethanmethanol, 1,3-oxazolidin-2-one, 3-(2-hydroxyethyl)-1,3-oxazolidin-2-one, 1,3-dioxan-2-one or a mixture thereof.

It is also possible to use any suitable mixture of surface-postcrosslinkers. It is particularly favorable to use mixtures of 1,3-dioxolan-2-on (ethylene carbonate) and 1,3-oxazolidin-2-ones. Such mixtures are obtainable by mixing and partly reacting of 1,3-dioxolan-2-on (ethylene carbonate) with the corresponding 2-amino-alcohol (e.g. 2-aminoethanol) and may comprise ethylene glycol from the reaction.

It is preferred that at least one alkylene carbonate is used as surface-postcrosslinker. Suitable alkylene carbonates are 1,3-dioxolan-2-on (ethylene carbonate), 4-methyl-1,3-dioxolan-2-on (propylene carbonate), 4,5-dimethyl-1,3-dioxolan-2-on, 4,4-dimethyl-1,3-dioxolan-2-on, 4-ethyl-1,3-dioxolan-2-on, 4-hydroxymethyl-1,3-dioxolan-2-on (glycerine carbonate), 1,3-dioxane-2-on (trimethylene carbonate), 4-methyl-1,3-dioxane-2-on, 4,6-dimethyl-1,3-dioxane-2-on and 1,3-dioxepan-2-on, preferably 1,3-dioxolan-2-on (ethylene carbonate) and 1,3-dioxane-2-on (trimethylene carbonate), most preferably 1,3-dioxolan-2-on (ethylene carbonate).

The amount of surface-postcrosslinker is preferably from 0.1 to 10% by weight, more preferably from 0.5 to 7.5% by weight, most preferably from 1 to 5% by weight, based in each case on the polymer.

The content of residual monomers in the water-absorbent polymer particles prior to the coating with the surface-postcrosslinker is in the range from 0.03 to 15% by weight, preferably from 0.05 to 12% by weight, more preferably from 0.1 to 10% by weight, even more preferably from 0.15 to 7.5% by weight, most preferably from 0.2 to 5% by weight, even most preferably from 0.25 to 2.5% by weight.

The moisture content of the water-absorbent polymer particles prior to the thermal surface-postcrosslinking is preferably from 1 to 20% by weight, more preferably from 2 to 15% by weight, most preferably from 3 to 10% by weight.

Polyvalent cations can be applied to the particle surface in addition to the surface-postcrosslinkers before, during or after the thermal surface-postcrosslinking.

The polyvalent cations usable in the process according to the invention are, for example, divalent cations such as the cations of zinc, magnesium, calcium, iron and strontium, trivalent cations such as the cations of aluminum, iron, chromium, rare earths and manganese, tetravalent cations such as the cations of titanium and zirconium, and mixtures thereof. Possible counterions are chloride, bromide, sulfate, hydrogensulfate, methanesulfate, carbonate, hydrogencarbonate, nitrate, hydroxide, phosphate, hydrogenphosphate, dihydrogenphosphate, glycophosphate and carboxylate, such as acetate, glycolate, tartrate, formiate, propionate, 3-hydroxypropionate, lactamide and lactate, and mixtures thereof. Aluminum sulfate, aluminum acetate, and aluminum lactate are preferred. Aluminum lactate is more preferred. Using the inventive process in combination with the use of aluminum lactate, water-absorbent polymer particles having an extremely high total liquid uptake at lower centrifuge retention capacities (CRC) can be prepared.

Apart from metal salts, it is also possible to use polyamines and/or polymeric amines as polyvalent cations. A single metal salt can be used as well as any mixture of the metal salts and/or the polyamines above.

Preferred polyvalent cations and corresponding anions are disclosed in WO 2012/045705 A1 and are expressly incorporated herein by reference. Preferred polyvinylamines are disclosed in WO 2004/024816 A1 and are expressly incorporated herein by reference.

The amount of polyvalent cation used is, for example, from 0.001 to 1.5% by weight, preferably from 0.005 to 1% by weight, more preferably from 0.02 to 0.8% by weight, based in each case on the polymer.

The addition of the polyvalent metal cation can take place prior, after, or cocurrently with the surface-postcrosslinking. Depending on the formulation and operating conditions employed it is possible to obtain a homogeneous surface coating and distribution of the polyvalent cation or an inhomogeneous typically spotty coating. Both types of coatings and any mixes between them are useful within the scope of the present invention.

The surface-postcrosslinking is typically performed in such a way that a solution of the surface-postcrosslinker is sprayed onto the hydrogel or the dry polymer particles. After the spraying, the polymer particles coated with the surface-postcrosslinker are dried thermally and cooled.

The spraying of a solution of the surface-postcrosslinker is preferably performed in mixers with moving mixing tools, such as screw mixers, disk mixers and paddle mixers. Suitable mixers are, for example, vertical Schugi Flexomix® mixers (Hosokawa Micron BV; Doetinchem; the Netherlands), Turbolizers® mixers (Hosokawa Micron BV; Doetinchem; the Netherlands), horizontal Pflugschar® plowshare mixers (Gebr. Lödige Maschinenbau GmbH; Paderborn; Germany), Vrieco-Nauta Continuous Mixers (Hosokawa Micron BV; Doetinchem; the Netherlands), Processall Mixmill Mixers (Processall Incorporated; Cincinnati; US) and Ruberg continuous flow mixers (Gebrüder Ruberg GmbH & Co KG, Nieheim, Germany). Ruberg continuous flow mixers and horizontal Pflugschar® plowshare mixers are preferred. The surface-postcrosslinker solution can also be sprayed into a fluidized bed.

The solution of the surface-postcrosslinker can also be sprayed on the water-absorbent polymer particles during the thermal posttreatment. In such case the surface-postcrosslinker can be added as one portion or in several portions along the axis of thermal posttreatment mixer. In one embodiment it is preferred to add the surface-postcrosslinker at the end of the thermal posttreatment step. As a particular advantage of adding the solution of the surface-postcrosslinker during the thermal posttreatment step it may be possible to eliminate or reduce the technical effort for a separate surface-postcrosslinker addition mixer.

The surface-postcrosslinkers are typically used as an aqueous solution. The addition of nonaqueous solvent can be used to improve surface wetting and to adjust the penetration depth of the surface-postcrosslinker into the polymer particles.

The thermal surface-postcrosslinking is preferably carried out in contact dryers, more preferably paddle dryers, most preferably disk dryers. Suitable driers are, for example, Hosokawa Bepex® horizontal paddle driers (Hosokawa Micron GmbH; Leingarten; Germany), Hosokawa Bepex® disk driers (Hosokawa Micron GmbH; Leingarten; Germany), Holo-Flite® dryers (Metso Minerals Industries Inc.; Danville; U.S.A.) and Nara paddle driers (NARA Machinery Europe; Frechen; Germany). Moreover, it is also possible to use fluidized bed dryers. In the latter case the reaction times may be shorter compared to other embodiments.

When a horizontal dryer is used then it is often advantageous to set the dryer up with an inclined angle of a few degrees vs. the earth surface in order to impart proper product flow through the dryer. The angle can be fixed or may be adjustable and is typically between 0 to 10 degrees, preferably 1 to 6 degrees, most preferably 2 to 4 degrees.

A contact dryer can be used that has two different heating zones in one apparatus. For example Nara paddle driers are available with just one heated zone or alternatively with two heated zones. The advantage of using a two or more heated zone dryer is that different phases of the thermal post-treatment and/or of the post-surface-crosslinking can be combined.

It is possible to use a contact dryer with a hot first heating zone which is followed by a temperature holding zone in the same dryer. This set up allows a quick rise of the product temperature and evaporation of surplus liquid in the first heating zone, whereas the rest of the dryer is just holding the product temperature stable to complete the reaction.

It is also possible to use a contact dryer with a warm first heating zone which is then followed by a hot heating zone. In the first warm zone the thermal post-treatment is affected or completed whereas the surface-postcrosslinking takes place in the subsequential hot zone.

Typically a paddle heater with just one temperature zone is employed.

A person skilled in the art will depending on the desired finished product properties and the available base polymer qualities from the polymerization step choose any one of these set ups.

The thermal surface-postcrosslinking can be effected in the mixer itself, by heating the jacket, blowing in warm air or steam. Equally suitable is a downstream dryer, for example a shelf dryer, a rotary tube oven or a heatable screw. It is particularly advantageous to mix and dry in a fluidized bed dryer.

Preferred thermal surface-postcrosslinking temperatures are usually in the range of 100-195° C., mostly in the range of 100 to 180° C., preferably from 120 to 170° C., more preferably from 130 to 165° C., most preferably from 140 to 160° C. The preferred residence time at this temperature in the reaction mixer or dryer is preferably at least 5 minutes, more preferably at least 20 minutes, most preferably at least 40 minutes, and typically at most 120 minutes.

It is preferable to cool the polymer particles after thermal surface-postcrosslinking. The cooling is preferably carried out in contact coolers, more preferably paddle coolers, most preferably disk coolers. Suitable coolers are, for example, Hosokawa Bepex® horizontal paddle coolers (Hosokawa Micron GmbH; Leingarten; Germany), Hosokawa Bepex® disk coolers (Hosokawa Micron GmbH; Leingarten; Germany), Holo-Flite® coolers (Metso Minerals Industries Inc.; Danville; U.S.A.) and Nara paddle coolers (NARA Machinery Europe; Frechen; Germany). Moreover, it is also possible to use fluidized bed coolers.

In the cooler the polymer particles are cooled to temperatures in the range from 20 to 150° C., preferably from 40 to 120° C., more preferably from 60 to 100° C., most preferably from 70 to 90° C. Cooling using warm water is preferred, especially when contact coolers are used.

Coating

To improve the properties, the water-absorbent polymer particles can be coated and/or optionally moistened. The internal fluidized bed, the external fluidized bed and/or the external mixer used for the thermal posttreatment and/or a separate coater (mixer) can be used for coating of the water-absorbent polymer particles. Further, the cooler and/or a separate coater (mixer) can be used for coating/moistening of the surface-postcrosslinked water-absorbent polymer particles. Suitable coatings for controlling the acquisition behavior and improving the permeability (SFC or GBP) are, for example, inorganic inert substances, such as water-insoluble metal salts, organic polymers, cationic polymers, anionic polymers and polyvalent metal cations. Suitable coatings for improving the color stability are, for example reducing agents, chelating agents and anti-oxidants. Suitable coatings for dust binding are, for example, polyols. Suitable coatings against the undesired caking tendency of the polymer particles are, for example, fumed silica, such as Aerosil® 200, and surfactants, such as Span® 20 and Plantacare® 818 UP. Preferred coatings are aluminium dihydroxy monoacetate, aluminium sulfate, aluminium lactate, aluminium 3-hydroxypropionate, zirconium acetate, citric acid or its water soluble salts, di- and mono-phosphoric acid or their water soluble salts, Blancolen®, Brüggolite® FF7, Cublen®, Span® 20 and Plantacare® 818 UP.

If salts of the above acids are used instead of the free acids then the preferred salts are alkali-metal, earth alkali metal, aluminum, zirconium, titanium, zinc and ammonium salts.

Under the trade name Cublen® (Zschimmer & Schwarz Mohsdorf GmbH & Co KG; Burgstädt; Germany) the following acids and/or their alkali metal salts (preferably Na and Ksalts) are available and may be used within the scope of the present invention for example to impart color-stability to the finished product:

1-Hydroxyethane-1,1-diphosphonic acid, Amino-tris(methylene phosphonic acid), Ethylenediamine-tetra(methylene phosphonic acid), Diethylenetriamine-penta(methylene phosphonic acid), Hexamethylene diamine-tetra(methylenephosphonic acid), Hydroxyethyl-aminodi(methylene phosphonic acid), 2-Phosphonobutane-1,2,4-tricarboxylic acid, Bis(hexamethylenetriamine penta(methylene phosphonic acid).

Most preferably 1-Hydroxyethane-1,1-diphosphonic acid or its salts with sodium, potassium, or ammonium are employed. Any mixture of the above Cublenes® can be used.

Alternatively, any of the chelating agents described before for use in the polymerization can be coated onto the finished product.

Suitable inorganic inert substances are silicates such as montmorillonite, kaolinite and talc, zeolites, activated carbons, polysilicic acids, magnesium carbonate, calcium carbonate, calcium phosphate, aluminum phosphate, barium sulfate, aluminum oxide, titanium dioxide and iron(II) oxide. Preference is given to using polysilicic acids, which are divided between precipitated silicas and fumed silicas according to their mode of preparation. The two variants are commercially available under the names Silica FK, Sipernat®, Wessalon® (precipitated silicas) and Aerosil® (fumed silicas) respectively. The inorganic inert substances may be used as dispersion in an aqueous or water-miscible dispersant or in substance.

When the water-absorbent polymer particles are coated with inorganic inert substances, the amount of inorganic inert substances used, based on the water-absorbent polymer particles, is preferably from 0.05 to 5% by weight, more preferably from 0.1 to 1.5% by weight, most preferably from 0.3 to 1% by weight.

Suitable organic polymers are polyalkyl methacrylates or thermoplastics such as polyvinyl chloride, waxes based on polyethylene, polypropylene, polyamides or polytetrafluoroethylene. Other examples are styrene-isoprene-styrene block-copolymers or styrenebutadiene-styrene block-copolymers. Another example are silanole-group bearing polyvinylalcohols available under the trade name Poval® R (Kuraray Europe GmbH; Frankfurt; Germany).

Suitable cationic polymers are polyalkylenepolyamines, cationic derivatives of polyacrylamides, polyethyleneimines and polyquaternary amines.

Polyquaternary amines are, for example, condensation products of hexamethylenediamine, dimethylamine and epichlorohydrin, condensation products of dimethylamine and epichlorohydrin, copolymers of hydroxyethylcellulose and diallyldimethylammonium chloride, copolymers of acrylamide and α-methacryloyloxyethyltrimethylammonium chloride, condensation products of hydroxyethylcellulose, epichlorohydrin and trimethylamine, homopolymers of diallyldimethylammonium chloride and addition products of epichlorohydrin to amidoamines. In addition, polyquaternary amines can be obtained by reacting dimethyl sulfate with polymers such as polyethyleneimines, copolymers of vinylpyrrolidone and dimethylaminoethyl methacrylate or copolymers of ethyl methacrylate and diethylaminoethyl methacrylate. The polyquaternary amines are available within a wide molecular weight range.

However, it is also possible to generate the cationic polymers on the particle surface, either through reagents which can form a network with themselves, such as addition products of epichlorohydrin to polyamidoamines, or through the application of cationic polymers which can react with an added crosslinker, such as polyamines or polyimines in combination with polyepoxides, polyfunctional esters, polyfunctional acids or polyfunctional (meth)acrylates.

It is possible to use all polyfunctional amines having primary or secondary amino groups, such as polyethyleneimine, polyallylamine and polylysine. The liquid sprayed by the process according to the invention preferably comprises at least one polyamine, for example polyvinylamine or a partially hydrolyzed polyvinylformamide.

The cationic polymers may be used as a solution in an aqueous or water-miscible solvent, as dispersion in an aqueous or water-miscible dispersant or in substance.

When the water-absorbent polymer particles are coated with a cationic polymer, the use amount of cationic polymer based on the water-absorbent polymer particles is usually not less than 0.001% by weight, typically not less than 0.01% by weight, preferably from 0.1 to 15% by weight, more preferably from 0.5 to 10% by weight, most preferably from 1 to 5% by weight.

Suitable anionic polymers are polyacrylates (in acidic form or partially neutralized as salt), copolymers of acrylic acid and maleic acid available under the trade name Sokalan® (BASF SE; Ludwigshafen; Germany), and polyvinylalcohols with built in ionic charges available under the trade name Poval® K (Kuraray Europe GmbH; Frankfurt; Germany).

Suitable polyvalent metal cations are Mg²⁺, Ca²⁺, Al³⁺, Sc³⁺, Ti⁴⁺, Mn²⁺, Fe^(2+/3+), Co²⁺, Ni²⁺, Ce^(+/2+), Zn²⁺, Y³⁺, Zr⁴⁺, Ag⁺, La³⁺, Ce⁴⁺, Hf⁴⁺ and Au^(+/3+); preferred metal cations are Mg²⁺, Ca²⁺, Al³⁺, Ti⁴⁺, Zr⁴⁺ and La³⁺; particularly preferred metal cations are Al³⁺, Ti⁴⁺ and Zr⁴⁺. The metal cations may be used either alone or in a mixture with one another. Suitable metal salts of the metal cations mentioned are all of those which have a sufficient solubility in the solvent to be used. Particularly suitable metal salts have weakly complexing anions, such as chloride, hydroxide, carbonate, acetate, formiate, propionate, nitrate, sulfate and methanesulfate. The metal salts are preferably used as a solution or as a stable aqueous colloidal dispersion. The solvents used for the metal salts may be water, alcohols, ethylenecarbonate, propylenecarbonate, dimethylformamide, dimethyl sulfoxide and mixtures thereof. Particular preference is given to water and water/alcohol mixtures, such as water/methanol, water/isopropanol, water/1,3-propanediole, water/1,2-propandiole/1,4-butanediole or water/propylene glycol.

When the water-absorbent polymer particles are coated with a polyvalent metal cation, the amount of polyvalent metal cation used, based on the water-absorbent polymer particles, is preferably from 0.05 to 5% by weight, more preferably from 0.1 to 1.5% by weight, most preferably from 0.3 to 1% by weight.

Suitable reducing agents are, for example, sodium sulfite, sodium hydrogensulfite (sodium bisulfite), sodium dithionite, sulfinic acids and salts thereof, ascorbic acid, sodium hypophosphite, sodium phosphite, and phosphinic acids and salts thereof. Preference is given, however, to salts of hypophosphorous acid, for example sodium hypophosphite, salts of sulfinic acids, for example the disodium salt of 2-hydroxy-2-sulfinatoacetic acid, and addition products of aldehydes, for example the disodium salt of 2-hydroxy-2-sulfonatoacetic acid. The reducing agent used can be, however, a mixture of the sodium salt of 2-hydroxy-2-sulfinatoacetic acid, the disodium salt of 2-hydroxy-2-sulfonatoacetic acid and sodium bisulfite. Such mixtures are obtainable as Brüggolite® FF6 and Brüggolite® FF7 (Brüggemann Chemicals; Heilbronn; Germany). Also useful is the purified 2-hydroxy-2-sulfonatoacetic acid and its sodium salts, available under the trade name Blancolen® from the same company.

The reducing agents are typically used in the form of a solution in a suitable solvent, preferably water. The reducing agent may be used as a pure substance or any mixture of the above reducing agents may be used.

When the water-absorbent polymer particles are coated with a reducing agent, the amount of reducing agent used, based on the water-absorbent polymer particles, is preferably from 0.01 to 5% by weight, more preferably from 0.05 to 2% by weight, most preferably from 0.1 to 1% by weight.

Suitable polyols are polyethylene glycols having a molecular weight of from 400 to 20000 g/mol, polyglycerol, 3- to 100-tuply ethoxylated polyols, such as trimethylolpropane, glycerol, sorbitol, mannitol, inositol, pentaerythritol and neopentyl glycol. Particularly suitable polyols are 7- to 20-tuply ethoxylated glycerol or trimethylolpropane, for example Polyol TP 70® (Perstorp AB, Perstorp, Sweden). The latter have the advantage in particular that they lower the surface tension of an aqueous extract of the water-absorbent polymer particles only insignificantly. The polyols are preferably used as a solution in aqueous or water-miscible solvents.

The polyol can be added before, during, or after surface-crosslinking. Preferably it is added after surface-cross linking. Any mixture of the above listed polyols may be used.

When the water-absorbent polymer particles are coated with a polyol, the use amount of polyol, based on the water-absorbent polymer particles, is preferably from 0.005 to 2% by weight, more preferably from 0.01 to 1% by weight, most preferably from 0.05 to 0.5% by weight.

The coating is preferably performed in mixers with moving mixing tools, such as screw mixers, disk mixers, paddle mixers and drum coater. Suitable mixers are, for example, horizontal Pflugschar® plowshare mixers (Gebr. Lödige Maschinenbau GmbH; Paderborn; Germany), Vrieco-Nauta Continuous Mixers (Hosokawa Micron BV; Doetinchem; the Netherlands), Processall Mixmill Mixers (Processall Incorporated; Cincinnati; US) and Ruberg continuous flow mixers (Gebrüder Ruberg GmbH & Co KG, Nieheim, Germany). Moreover, it is also possible to use a fluidized bed for mixing.

Agglomeration

The water-absorbent polymer particles can further selectively be agglomerated. The agglomeration can take place after the polymerization, the thermal postreatment, the thermal surface-postcrosslinking or the coating.

Useful agglomeration assistants include water and water-miscible organic solvents, such as alcohols, tetrahydrofuran and acetone; water-soluble polymers can be used in addition.

For agglomeration a solution comprising the agglomeration assistant is sprayed onto the water-absorbing polymeric particles. The spraying with the solution can, for example, be carried out in mixers having moving mixing implements, such as screw mixers, paddle mixers, disk mixers, plowshare mixers and shovel mixers. Useful mixers include for example Lödige® mixers, Bepex® mixers, Nauta® mixers, Processall® mixers and Schugi® mixers. Vertical mixers are preferred. Fluidized bed apparatuses are particularly preferred.

Combination of thermal posttreatment, surface-postcrosslinking and optionally coating

It is preferred that the steps of thermal posttreatment and thermal surface-postcrosslinking are combined in one process step. Such combination allows the use of low cost equipment and moreover the process can be run at low temperatures, that is cost-efficient and avoids discoloration and loss of performance properties of the finished product by thermal degradation.

The mixer may be selected from any of the equipment options cited in the thermal post-treatment section. Ruberg continuous flow mixers, Becker shovel mixers and Pflugschar® plowshare mixers are preferred.

It is particular preferred that the surface-postcrosslinking solution is sprayed onto the water-absorbent polymer particles under agitation.

Following the thermal posttreatment/surface-postcrosslinking the water-absorbent polymer particles are dried to the desired moisture level and for this step any dryer cited in the surface-postcrosslinking section may be selected. However, as only drying needs to be accomplished in this particular preferred embodiment it is possible to use simple and low cost heated contact dryers like a heated screw dryer, for example a Holo-Flite® dryer (Metso Minerals Industries Inc.; Danville; U.S.A.). Alternatively a fluidized bed may be used. In cases where the product needs to be dried with a predetermined and narrow residence time it is possible to use torus disc dryers or paddle dryers, for example a Nara paddle dryer (NARA Machinery Europe; Frechen; Germany).

In a preferred embodiment of the present invention, polyvalent cations cited in the surface-postcrosslinking section are applied to the particle surface before, during or after addition of the surface-postcrosslinker by using different addition points along the axis of a horizontal mixer.

It is very particular preferred that the steps of thermal post-treatment, surface-postcrosslinking, and coating are combined in one process step. Suitable coatings are cationic polymers, surfactants, and inorganic inert substances that are cited in the coating section. The coating agent can be applied to the particle surface before, during or after addition of the surface-postcrosslinker also by using different addition points along the axis of a horizontal mixer.

The polyvalent cations and/or the cationic polymers can act as additional scavengers for residual surface-postcrosslinkers. It is preferred that the surface-postcrosslinkers are added prior to the polyvalent cations and/or the cationic polymers to allow the surface-postcrosslinker to react first.

The surfactants and/or the inorganic inert substances can be used to avoid sticking or caking during this process step under humid atmospheric conditions. Preferred surfactants are non-ionic and amphoteric surfactants. Preferred inorganic inert substances are precipitated silicas and fumed silcas in form of powder or dispersion.

The amount of total liquid used for preparing the solutions/dispersions is typically from 0.01% to 25% by weight, preferably from 0.5% to 12% by weight, more preferably from 2% to 7% by weight, most preferably from 3% to 6% by weight, in respect to the weight amount of water-absorbent polymer particles to be processed.

Preferred embodiments are depicted in FIGS. 1 to 15.

FIG. 1: Process scheme

FIG. 2: Process scheme using dry air

FIG. 3: Arrangement of the T_outlet measurement

FIG. 4: Arrangement of the dropletizer units with 3 droplet plates

FIG. 5: Arrangement of the dropletizer units with 9 droplet plates

FIG. 6: Arrangement of the dropletizer units with 9 droplet plates

FIG. 7: Dropletizer unit (longitudinal cut)

FIG. 8: Dropletizer unit (cross sectional view)

FIG. 9: Bottom of the internal fluidized bed (top view)

FIG. 10: openings in the bottom of the internal fluidized bed

FIG. 11: Rake stirrer for the intern fluidized bed (top view)

FIG. 12: Rake stirrer for the intern fluidized bed (cross sectional view)

FIG. 13: Process scheme (surface-postcrosslinking)

FIG. 14: Process scheme (surface-postcrosslinking and coating)

FIG. 15: Contact dryer for surface-postcrosslnking

The reference numerals have the following meanings:

-   -   1 Drying gas inlet pipe     -   2 Drying gas amount measurement     -   3 Gas distributor     -   4 Dropletizer unit(s)     -   4 a Dropletizer unit     -   4 b Dropletizer unit     -   4 c Dropletizer unit     -   5 Reaction zone (cylindrical part of the spray dryer)     -   6 Cone     -   7 T_outlet measurement     -   8 Tower offgas pipe     -   9 Dust separation unit     -   10 Ventilator     -   11 Quench nozzles     -   12 Condenser column, counter current cooling     -   13 Heat exchanger     -   14 Pump     -   15 Pump     -   16 Water outlet     -   17 Ventilator     -   18 Offgas outlet     -   19 Nitrogen inlet     -   20 Heat exchanger     -   21 Ventilator     -   22 Heat exchanger     -   24 Water loading measurement     -   25 Conditioned internal fluidized bed gas     -   26 Internal fluidized bed product temperature measurement     -   27 Internal fluidized bed     -   28 Rotary valve     -   29 Sieve     -   30 End product     -   31 Static mixer     -   32 Static mixer     -   33 Initiator feed     -   34 Initiator feed     -   35 Monomer feed     -   36 Fine particle fraction outlet to rework     -   37 Gas drying unit     -   38 Monomer separator unit     -   39 Gas inlet pipe     -   40 Gas outlet pipe     -   41 Water outlet from the gas drying unit to condenser column     -   42 Waste water outlet     -   43 T_outlet measurement (average temperature out of 3         measurements around tower circumference)     -   45 Monomer premixed with initiator feed     -   46 Spray dryer tower wall     -   47 Dropletizer unit outer pipe     -   48 Dropletizer unit inner pipe     -   49 Dropletizer cassette     -   50 Teflon block     -   51 Valve     -   52 Monomer premixed with initiator feed inlet pipe connector     -   53 Droplet plate     -   54 Counter plate     -   55 Flow channels for temperature control water     -   56 Dead volume free flow channel for monomer solution     -   57 Dropletizer cassette stainless steel block     -   58 Bottom of the internal fluidized bed with four segments     -   59 Split openings of the segments     -   60 Rake stirrer     -   61 Prongs of the rake stirrer     -   62 Mixer     -   63 Optional coating feed     -   64 Postcrosslinker feed     -   65 Thermal dryer (surface-postcrosslinking)     -   66 Cooler     -   67 Optional coating/water feed     -   68 Coater     -   69 Coating/water feed     -   70 Base polymer feed     -   71 Discharge zone     -   72 Weir opening     -   73 Weir plate     -   74 Weir height 100%     -   75 Weir height 50%     -   76 Shaft     -   77 Discharge cone     -   78 Inclination angle α     -   79 Temperature sensors (Ti to T₆)     -   80 Paddle (shaft offset 90°)

The drying gas is fed via a gas distributor (3) at the top of the spray dryer as shown in FIG. 1. The drying gas is partly recycled (drying gas loop) via a baghouse filter or cyclone unit (9) and a condenser column (12). The pressure inside the spray dryer is below ambient pressure.

The spray dryer outlet temperature is preferably measured at three points around the circumference at the end of the cylindrical part as shown in FIG. 3. The single measurements (43) are used to calculate the average cylindrical spray dryer outlet temperature.

In one preferred embodiment a monomer separator unit (38) is used for recycling of the monomers from the condenser column (12) into the monomer feed (35). This monomer separator unit is for example especially a combination of micro-, ultra-, nanofiltration and osmose membrane units, to separate the monomer from water and polymer particles. Suitable membrane separator systems are described, for example, in the monograph “Membranen: Grundlagen, Verfahren und Industrielle Anwendungen”, K. Ohlrogge and K. Ebert, Wiley-VCH, 2012 (ISBN: 978-3-527-66033-9).

The product accumulated in the internal fluidized bed (27). Conditioned internal fluidized bed gas is fed to the internal fluidized bed (27) via line (25). The relative humidity of the internal fluidized bed gas is preferably controlled by the temperature in the condenser column (12) and using the Mollier diagram.

The spray dryer offgas is filtered in a dust separation unit (9) and sent to a condenser column (12) for quenching/cooling. After dust separation (9) a recuperation heat exchanger system for preheating the gas after the condenser column (12) can be used. The dust separation unit (9) may be heat-traced on a temperature of preferably from 80 to 180° C., more preferably from 90 to 150° C., most preferably from 100 to 140° C.

Example for the dust separation unit are baghouse filter, membranes, cyclones, dust compactors and for examples described, for example, in the monographs “Staubabscheiden”, F. Löffler, Georg Thieme Verlag, Stuttgart, 1988 (ISBN 978-3137122012) and “Staubabscheidung mit Schlauchfiltern und Taschenfiltern”, F. Löffler, H. Dietrich and W. Flatt, Vieweg, Braunschweig, 1991 (ISBN 978-3540670629).

Most preferable are cyclones, for example, cyclones/centrifugal separators of the types ZSA/ZSB/ZSC from LTG Aktiengesellschaft and cyclone separators from Ventilatorenfabrik Oelde GmbH, Camfil Farr International and MikroPul GmbH.

Excess water is pumped out of the condenser column (12) by controlling the (constant) filling level in the condenser column (12). The water in the condenser column (12) is pumped counter-current to the gas via quench nozzles (11) and cooled by a heat exchanger (13) so that the temperature in the condenser column (12) is preferably from 40 to 71° C., more preferably from 46 to 69° C., most preferably from 49 to 65° C. and more even preferably from 51 to 60° C. The water in the condenser column (12) is set to an alkaline pH by dosing a neutralizing agent to wash out vapors of monomer a). Aqueous solution from the condenser column (12) can be sent back for preparation of the monomer solution.

The condenser column offgas may be split to the gas drying unit (37) and the conditioned internal fluidized bed gas (27).

The principle of a gas drying unit is described in the monograph “Leitfaden für Lüftungsund Klimaanlagen—Grundlagen der Thermodynamik Komponenten einer Vollklimaanlage Normen and Vorschriften”, L. Keller, Oldenbourg Industrieverlag, 2009 (ISBN 978-3835631656).

As gas drying unit can be used, for example, an air gas cooling system in combination with a gas mist eliminators or droplet separator (demister), for examples, droplet vane type separator for horizontal flow (e.g. type DH 5000 from Munters AB, Sweden) or vertical flow (e.g. type DV 270 from Munters AB, Sweden). Vane type demisters remove liquid droplets from continuous gas flows by inertial impaction. As the gas carrying entrained liquid droplets moves through the sinusoidal path of a vane, the higher density liquid droplets cannot follow and as a result, at every turn of the vane blades, these liquid droplets impinge on the vane surface. Most of the droplets adhere to the vane wall. When a droplet impinges on the vane blade at the same location, coalescence occurs. The coalesced droplets then drain down due to gravity.

As air gas cooling system, any gas/gas or gas/liquid heat exchanger can be used. Preferred are sealed plate heat exchangers.

In one embodiment dry air can be used as feed for the gas distributor (3). If air used as gas, then air can be transported via air inlet pipe (39) and can be dried in the gas drying unit (37), as described before. After the condenser column (12), the air, which not used for the internal fluidized bed is transported via the outlet pipe outside (40) of the plant as shown in FIG. 2.

The water, which is condensed in the gas drying unit (37) can be partially used as wash water for the condenser column (12) or disposed.

The gas temperatures are controlled via heat exchangers (20) and (22). The hot drying gas is fed to the cocurrent spray dryer via gas distributor (3). The gas distributor (3) consists preferably of a set of plates providing a pressure drop of preferably 1 to 100 mbar, more preferably 2 to 30 mbar, most preferably 4 to 20 mbar, depending on the drying gas amount. Turbulences and/or a centrifugal velocity can also be introduced into the drying gas if desired by using gas nozzles or baffle plates.

Conditioned internal fluidized bed gas is fed to the internal fluidized bed (27) via line (25). The steam content of the fluidized bed gas can be controlled by the temperature in the condenser column (12). The product holdup in the internal fluidized bed (27) can be controlled via rotational speed of the rotary valve (28).

The amount of gas in the internal fluidized bed (27) is selected so that the particles move free and turbulent in the internal fluidized bed (27). The product height in the internal fluidized bed (27) is with gas preferably at least 10%, more preferably at least 20%, more preferably at least 30%, even more preferably at least 40% higher than without gas.

The product is discharged from the internal fluidized bed (27) via rotary valve (28). The product holdup in the internal fluidized bed (27) can be controlled via rotational speed of the rotary valve (28). The sieve (29) is used for sieving off overs/lumps.

The monomer solution is preferably prepared by mixing first monomer a) with a neutralization agent and secondly with crosslinker b). The temperature during neutralization is controlled to preferably from 5 to 60° C., more preferably from 8 to 40° C., most preferably from 10 to 30° C., by using a heat exchanger and pumping in a loop. A filter unit is preferably used in the loop after the pump. The initiators are metered into the monomer solution upstream of the dropletizer by means of static mixers (31) and (32) via lines (33) and (34) as shown in FIG. 1 and FIG. 2. Preferably a peroxide solution having a temperature of preferably from 5 to 60° C., more preferably from 10 to 50° C., most preferably from 15 to 40° C., is added via line (33) and preferably an azo initiator solution having a temperature of preferably from 2 to 30° C., more preferably from 3 to 15° C., most preferably from 4 to 8° C., is added via line (34). Each initiator is preferably pumped in a loop and dosed via control valves to each dropletizer unit. A second filter unit is preferably used after the static mixer (32). The mean residence time of the monomer solution admixed with the full initiator package in the piping before dropletization is preferably less than 60 s, more preferably less than 30 s, most preferably less than 10 s.

For dosing the monomer solution into the top of the spray dryer preferably three dropletizer units are used as shown in FIG. 4. However, any number of dropletizers can be used that is required to optimize the throughput of the process and the quality of the product. Hence, in the present invention at least one dropletizer is employed, and as many dropletizers as geometrically allowed may be used.

A dropletizer unit consists of an outer pipe (47) having an opening for the dropletizer cassette (49) as shown in FIG. 7. The dropletizer cassette (49) is connected with an inner pipe (48). The inner pipe (48) having a PTFE block (50) at the end as sealing can be pushed in and out of the outer pipe (51) during operation of the process for maintenance purposes.

The temperature of the dropletizer cassette (57) is controlled to preferably 5 to 80° C., more preferably 10 to 70° C., most preferably 30 to 60° C., by water in flow channels (55) as shown in FIG. 8.

The dropletizer cassette has preferably from 10 to 2000 bores, more preferably from 50 to 1500 bores, most preferably from 100 to 1000 bores. The diameter of the bores size area is 1900 to 22300 μm², more preferably from 7800 to 20100 μm², most preferably from 11300 to 17700 μm². The bores can be of circular, rectangular, triangular or any other shape. Circular bores are preferred with a bore size from 50 to 170 μm, more preferably from 100 to 160 μm, most preferably from 120 to 150 μm. The ratio of bore length to bore diameter is preferably from 0.5 to 10, more preferably from 0.8 to 5, most preferably from 1 to 3. The droplet plate (53) can have a greater thickness than the bore length when using an inlet bore channel. The droplet plate (53) is preferably long and narrow as disclosed in WO 2008/086976 A1. Multiple rows of bores per droplet plate can be used, preferably from 1 to 20 rows, more preferably from 2 to 5 rows.

The dropletizer cassette (57) consists of a flow channel (56) having essential no stagnant volume for homogeneous distribution of the premixed monomer and initiator solutions and two droplet plates (53). The droplet plates (53) have an angled configuration with an angle of preferably from 1 to 90°, more preferably from 3 to 45°, most preferably from 5 to 20°. Each droplet plate (53) is preferably made of a heat and/or chemically resistant material, such as stainless steel, polyether ether ketone, polycarbonate, polyarylsulfone, such as polysulfone, or polyphenylsulfone, or fluorous polymers, such as perfluoroalkoxyethylene, polytetrafluoroethylene, polyvinylidenfluorid, ethylene-chlorotrifluoroethylene copolymers, ethylene-tetrafluoroethylene copolymers and fluorinated polyethylene. Coated droplet plates as disclosed in WO 2007/031441 A1 can also be used. The choice of material for the droplet plate is not limited except that droplet formation must work and it is preferable to use materials which do not catalyze the start of polymerization on its surface.

The arrangement of dropletizer cassettes is preferably rotationally symmetric or evenly distributed in the spray dryer (for example see FIGS. 3 to 5).

In a preferred embodiment the angle configuration of the droplet plate (53) is in the middle lower then outside, for example: 4a=3°, 4b=5° and 4c=8° (FIG. 5).

The throughput of monomer including initiator solutions per dropletizer unit is preferably from 10 to 4000 kg/h, more preferably from 100 to 1000 kg/h, most preferably from 200 to 600 kg/h. The throughput per bore is preferably from 0.1 to 10 kg/h, more preferably from 0.5 to 5 kg/h, most preferably from 0.7 to 2 kg/h.

The start-up of the cocurrent spray dryer (5) can be done in the following sequence:

-   -   starting the condenser column (12),     -   starting the ventilators (10) and (17),     -   starting the heat exchanger (20),     -   heating up the drying gas loop up to 95° C.,     -   starting the nitrogen feed via the nitrogen inlet (19),     -   waiting until the residual oxygen is below 4% by weight,     -   heating up the drying gas loop,     -   at a temperature of 105° C. starting the water feed (not shown)         and     -   at target temperature stopping the water feed and starting the         monomer feed via dropletizer unit (4)

The shut-down of the cocurrent spray dryer (5) can be done in the following sequence:

-   -   stopping the monomer feed and starting the water feed (not         shown),     -   shut-down of the heat exchanger (20),     -   cooling the drying gas loop via heat exchanger (13),     -   at a temperature of 105° C. stopping the water feed,     -   at a temperature of 60° C. stopping the nitrogen feed via the         nitrogen inlet (19) and     -   feeding air into the drying gas loop (not shown)

To prevent damages the cocurrent spray dryer (5) must be heated up and cooled down very carefully. Any quick temperature change must be avoided.

The openings in the bottom of the internal fluidized bed may be arranged in a way that the water-absorbent polymer particles flow in a cycle as shown in FIG. 9. The bottom shown in FIG. 9 comprises of four segments (58). The openings (59) in the segments (58) are in the shape of slits that guides the passing gas stream into the direction of the next segment (58). FIG. 10 shows an enlarged view of the openings (59).

The opening may have the shape of holes or slits. The diameter of the holes is preferred from 0.1 to 10 mm, more preferred from 0.2 to 5 mm, most preferred from 0.5 to 2 mm. The slits have a length of preferred from 1 to 100 mm, more preferred from 2 to 20 mm, most preferred from 5 to 10 mm, and a width of preferred from 0.5 to 20 mm, more preferred from 1 to 10 mm, most preferred from 2 to 5 mm.

FIG. 11 and FIG. 12 show a rake stirrer (60) that may be used in the internal fluidized bed. The prongs (61) of the rake have a staggered arrangement. The speed of rake stirrer is preferably from 0.5 to 20 rpm, more preferably from 1 to 10 rpm most preferably from 2 to 5 rpm.

For start-up the internal fluidized bed may be filled with a layer of water-absorbent polymer particles, preferably 5 to 50 cm, more preferably from 10 to 40 cm, most preferably from 15 to 30 cm.

The surface-postcrosslinked water-absorbent polymer particles having a sphericity of at least 0.89, a centrifuge retention capacity of at least 34 g/g, an AUL (0.3 psi 21 g cm⁻²) (EDANA 442.2-02) of at least 30 g/g and a level of extractable constituents of less than 10% by weight.

The surface-postcrosslinked water-absorbent polymer particles have a centrifuge retention capacity (CRC) from 34 to 75 g/g, preferably from 36 to 65 g/g, more preferably from 39 to 60 g/g, most preferably from 40 to 55 g/g.

The surface-postcrosslinked water-absorbent polymer particles have an absorbency under a load AUL (0.3 psi 21 g cm⁻²) from 30 to 50 g/g, preferably from 32 to 45 g/g.

It is particular advantageous that the surface-postcrosslinked water-absorbent polymer particles exhibit a very high centrifuge retention capacity (CRC) and an absorption under load (AUL, 21 g/cm²), and that the sum of these parameters (=CRC+AUL) is at least 65 g/g, preferably at least 70 g/g, most preferably at least 75 g/g,

The water-absorbent polymer particles have a level of extractable constituents of less than 10% by weight, preferably less than 9% by weight, more preferably less than 8% by weight, most preferably less than 6% by weight.

The water-absorbent polymer particles suited for the present invention have a mean sphericity from 0.80 to 0.95, preferably from 0.82 to 0.93, more preferably from 0.84 to 0.91, most preferably from 0.85 to 0.90. The sphericity (SPHT) is defined as

${{SPHT} = \frac{4\; \pi \; A}{U^{2}}},$

where A is the cross-sectional area and U is the cross-sectional circumference of the polymer particles. The mean sphericity is the volume-average sphericity.

The mean sphericity can be determined, for example, with the Camsizer® image analysis system (Retsch Technolgy GmbH; Haan; Germany):

For the measurement, the product is introduced through a funnel and conveyed to the falling shaft with a metering channel. While the particles fall past a light wall, they are recorded selectively by a camera. The images recorded are evaluated by the software in accordance with the parameters selected.

To characterize the roundness, the parameters designated as sphericity in the program are employed. The parameters reported are the mean volume-weighted sphericities, the volume of the particles being determined via the equivalent diameter xc_(min). To determine the equivalent diameter xc_(min), the longest chord diameter for a total of 32 different spatial directions is measured in each case. The equivalent diameter xc_(min) is the shortest of these 32 chord diameters. To record the particles, the so-called CCD-zoom camera (CAM-Z) is used. To control the metering channel, a surface coverage fraction in the detection window of the camera (transmission) of 0.5% is predefined.

Water-absorbent polymer particles with relatively low sphericity are obtained by reverse suspension polymerization when the polymer beads are agglomerated during or after the polymerization.

Water-absorbent polymer particles contained at least in the upper layer (91) of the absorbent core (absorbent paper) according to the present invention and the inventive fluid absorbent articles respectively have a content of hydrophobic solvent of preferably less than 0.005% by weight, more preferably less than 0.002% by weight and most preferably less than 0.001% by weight. The content of hydrophobic solvent can be determined by gas chromatography, for example by means of the headspace technique. A hydrophobic solvent within the scope of the present invention is either immiscible in water or only sparingly miscible. Typical examples of hydrophobic solvents are pentane, hexane, cyclohexane, toluene.

The water-absorbent polymer particles useful for the present invention have a dispersant content of typically less than 1% by weight, preferably less than 0.5% by weight, more preferably less than 0.1% by weight and most preferably less than 0.05% by weight.

Suitable water-absorbent polymer particles have a bulk density preferably from 0.6 to 1 g/cm³, more preferably from 0.65 to 0.95 g/cm³, most preferably from 0.7 to 0.9 g/cm³.

The average particle diameter of the water-absorbent particles useful for the present invention is preferably from 200 to 550 μm, more preferably from 250 to 500 μm, most preferably from 350 to 450 μm.

One kind of water-absorbent polymer particles can be mixed with other water-absorbent polymer particles prepared by other processes, i.e. solution polymerization.

C. Fluid-Absorbent Articles

The fluid-absorbent article comprises

-   -   (A) an upper liquid-pervious layer (89)     -   (B) a lower liquid-impervious layer (83)     -   (C) a fluid-absorbent core (80) between (89) and (83) comprising         -   at least two layers (91, 92), wherein each layer comprising             from 0 to 10% by weight a fibrous material and from 90 to             100% by weight water-absorbent polymer particles;         -   preferably from 0 to 5% by weight a fibrous material and             from 95 to 100% by weight water-absorbent polymer particles;         -   more preferably from 0% by weight a fibrous material and 100             by weight water-absorbent polymer particles;         -   based on the sum of water-absorbent polymer material and             fibrous material.     -   (D) an optional acquisition-distribution layer between (A) and         (C)     -   and     -   (E) other optional components.

Preferably the fluid-absorbent core between (89) and (83) comprising

an upper tissue layer (95), an upper layer comprising water-absorbent polymer particles (91) and a lower layer comprising water-absorbent polymer particles (92), at least one layer of nonwoven material (94) sandwiched between the upper layer (91) and lower layer (92).

Fluid-absorbent articles are understood to mean, for example, incontinence pads and incontinence briefs for adults or diapers and training pants for babies. Suitable fluid-absorbent articles including fluid-absorbent compositions comprising fibrous materials and optionally water-absorbent polymer particles to form fibrous webs or matrices for the substrates, layers, sheets and/or the fluid-absorbent core.

Suitable fluid-absorbent articles are composed of several layers whose individual elements must show preferably definite functional parameter such as dryness for the upper liquid-pervious layer (89), vapor permeability without wetting through for the lower liquid-impervious layer (83), a flexible, vapor permeable and thin fluid-absorbent core (80), showing fast absorption rates and being able to retain highest quantities of body fluids, and an optional acquisition-distribution layer between the upper layer (89) and the core (80), acting as transport and distribution layer of the discharged body fluids. These individual elements are combined such that the resultant fluid-absorbent article meets overall criteria such as flexibility, water vapour breathability, dryness, wearing comfort and protection on the user facing side, and concerning liquid retention, rewet and prevention of wet through on the garment side. The specific combination of these layers provides a fluid-absorbent article delivering both high protection levels as well as high comfort to the consumer.

The core-structure for fluid-absorbent products according to the invention is formed from absorbent paper. Absorbent paper usually is a sandwich structure comprising tissue, layers of water-absorbent polymer particles, and nonwovens. The different components preferably are connected by adhesives, ultrasonic bonding and/or heat bonding.

For fluid-absorbent articles it is advantageous especially in respect to fluid distribution to have acquisition-distribution layers. For fluid-absorbent articles that possess a fluid-absorbent core comprising very permeable water-absorbent polymer particles a small and thin acquisition-distribution layer can be used.

The acquisition-distribution layer acts as transport and distribution layer of the discharged body fluids and is typically optimized to affect efficient liquid distribution with the underlying fluid-absorbent core. Hence, for quick temporary liquid retention it provides the necessary void space while its area coverage of the underlying fluid-absorbent core must affect the necessary liquid distribution and is adopted to the ability of the fluid-absorbent core to quickly dewater the acquisition-distribution layer.

Methods to make fluid absorbent articles are for example described in the following publications and literature cited therein and are expressly incorporated into the present invention: EP 2 301 499 A1, EP 2 314 264 A1, EP 2 387 981 A1, EP 2 486 901 A1, EP 2 524 679 A1, EP 2 524 679 A1, EP 2 524 680 A1, EP 2 565 031 A1, U.S. Pat. No. 6,972,011, US 2011/0162989, US 2011/0270204, WO 2010/004894 A1, WO 2010/004895 A1, WO 2010/076857 A1, WO 2010/082373 A1, WO 2010/118409 A1, WO 2010/133529 A2, WO 2010/143635 A1, WO 2011/084981 A1, WO 2011/086841 A1, WO 2011/086842 A1, WO 2011/086843 A1, WO 2011/086844 A1, WO 2011/117997 A1, WO 2011/136087 A1, WO 2012/048879 A1, WO 2012/052173 A1 and WO 2012/052172 A1.

FIG. 16 is a schematical view of a fluid absorbent article

The fluid-absorbent article comprises an absorbent core (80) comprising at least two layers of water-absorbent polymer particles, top (91), bottom (92) sandwiched by at least two tissue layers, top 95 and bottom, 96 and at least one nonwoven (94) (e.g. high loft air thru bond nonwoven) sandwiched by the at least two layers of water-absorbent polymer particles (91, 92). The layers may be connected to each other e. g. by adhesive, ultrasonic bonding or any other suitable method. The total absorbent core (80) structure is optionally surrounded/wrapped by a further nonwoven sheet or tissue layer (86) also optionally connected by an adhesive to the sandwich structure.

Furthermore the absorbent article may comprise an acquisition distribution layer on top of the absorbent core (80) or core wrap (86) respectively below the upper liquid-pervious sheet or coverstock (89) (e. g. embossed spunbond nonwoven), and a lower liquid-impervious sheet (83). Leg cuffs (81) and some elastics (88) may be also present.

Liquid-Pervious Sheet or Liquid Pervious Layer (89)

The liquid-pervious sheet (A)(89) is the layer which is in direct contact with the skin. Thus, the liquid-pervious sheet is preferably compliant, soft feeling and non-irritating to the consumer's skin. Generally, the term “liquid-pervious” is understood thus permitting liquids, i.e. body fluids such as urine, menses and/or vaginal fluids to readily penetrate through its thickness. The principle function of the liquid-pervious sheet is the acquisition and transport of body fluids from the wearer towards the fluid-absorbent core. Typically liquid-pervious layers are formed from any materials known in the art such as nonwoven material, films or combinations thereof. Suitable liquid-pervious sheets (A)(89) consist of customary synthetic or semisynthetic fibers or bicomponent fibers or films of polyester, polyolefins, rayon or natural fibers or any combinations thereof. In the case of nonwoven materials, the fibers should generally be bound by binders such as polyacrylates. Additionally the liquid-pervious sheet may contain elastic compositions thus showing elastic characteristics allowing to be stretched in one or two directions.

Suitable synthetic fibers are made from polyvinyl chloride, polyvinyl fluoride, polytetrafluorethylene, polyvinylidene chloride, polyacrylics, polyvinyl acetate, polyethylvinyl acetate, non-soluble or soluble polyvinyl alcohol, polyolefins such as polyethylene, polypropylene, polyamides, polyesters, polyurethanes, polystyrenes and the like.

Examples for films are apertured formed thermoplastic films, apertured plastic films, hydro-formed thermoplastic films, reticulated thermoplastic films, porous foams, reticulated foams, and thermoplastic scrims.

Examples of suitable modified or unmodified natural fibers include cotton, bagasse, kemp, flax, silk, wool, wood pulp, chemically modified wood pulp, jute, rayon, ethyl cellulose, and cellulose acetate.

The fibrous material may comprise only natural fibers or synthetic fibers or any combination thereof. Preferred materials are polyester, rayon and blends thereof, polyethylene, and polypropylene. The fibrous material as a component of the fluid-absorbent compositions may be hydrophilic, hydrophobic or can be a combination of both hydrophilic and hydrophobic fibers. The selection of the ratio hydrophilic/hydrophobic and accordingly the amount of hydrophilic and hydrophobic fibers within fluid-absorbent composition will depend upon fluid handling properties and the amount of water-absorbent polymer particles of the resulting fluid-absorbent composition.

Examples for hydrophilic fibers are cellulosic fibers, modified cellulosic fibers, rayon, polyester fibers such as polyethylene terephthalate, hydrophilic nylon and the like. Hydrophilic fibers can also be obtained from hydrophobic fibers which are hydrophilized by e. g. surfactant-treating or silica-treating. Thus, hydrophilic thermoplastic fibers derived from polyolefins such as polypropylene, polyamides, polystyrenes or the like by surfactant-treating or silica-treating.

To increase the strength and the integrity of the upper-layer, the fibers should generally show bonding sites, which act as crosslinks between the fibers within the layer.

Technologies for consolidating fibers in a web are mechanical bonding, thermal bonding and chemical bonding. In the process of mechanical bonding the fibers are entangled mechanically, e.g., by water jets (spunlace) to give integrity to the web. Thermal bonding is carried out by means of raising the temperature in the presence of low-melting polymers. Examples for thermal bonding processes are spunbonding, through-air bonding and resin bonding.

Preferred means of increasing the integrity are thermal bonding, spunbonding, resin bonding, through-air bonding and/or spunlace.

In the case of thermal bonding, thermoplastic material is added to the fibers. Upon thermal treatment at least a portion of this thermoplastic material is melting and migrates to intersections of the fibers caused by capillary effects. These intersections solidify to bond sites after cooling and increase the integrity of the fibrous matrix. Moreover, in the case of chemically stiffened cellulosic fibers, melting and migration of the thermoplastic material has the effect of increasing the pore size of the resultant fibrous layer while maintaining its density and basis weight. Upon wetting, the structure and integrity of the layer remains stable. In summary, the addition of thermoplastic material leads to improved fluid permeability of discharged body fluids and thus to improved acquisition properties.

Suitable thermoplastic materials including polyolefins such as polyethylene and polypropylene, polyesters, copolyesters, polyvinyl acetate, polyethylvinyl acetate, polyvinyl chloride, polyvinylidene chloride, polyacrylics, polyamides, copolyamides, polystyrenes, polyurethanes and copolymers of any of the mentioned polymers.

Suitable thermoplastic fibers can be made from a single polymer that is a monocomponent fiber. Alternatively, they can be made from more than one polymer, e.g., bi-component or multicomponent fibers. The term “bicomponent fibers” refers to thermoplastic fibers that comprise a core fiber made from a different fiber material than the shell. Typically, both fiber materials have different melting points, wherein generally the sheath melts at lower temperatures. Bi-component fibers can be concentric or eccentric depending whether the sheath has a thickness that is even or uneven through the cross-sectional area of the bi-component fiber. Advantage is given for eccentric bi-component fibers showing a higher compressive strength at lower fiber thickness. Further bi-component fibers can show the feature “uncrimped” (unbent) or “crimped” (bent), further bi-component fibers can demonstrate differing aspects of surface lubricity.

Examples of bi-component fibers include the following polymer combinations: polyethylene/polypropylene, polyethylvinyl acetate/polypropylene, polyethylene/polyester, polypropylene/polyester, copolyester/polyester and the like.

Suitable thermoplastic materials have a melting point of lower temperatures that will damage the fibers of the layer; but not lower than temperatures, where usually the fluid-absorbent articles are stored. Preferably the melting point is between about 75° C. and 175° C. The typical length of thermoplastic fibers is from about 0.4 to 6 cm, preferably from about 0.5 to 1 cm. The diameter of thermoplastic fibers is defined in terms of either denier (grams per 9000 meters) or dtex (grams per 10 000 meters). Typical thermoplastic fibers have a dtex in the range from about 1.2 to 20, preferably from about 1.4 to 10.

A further mean of increasing the integrity of the fluid-absorbent composition is the spunbonding technology. The nature of the production of fibrous layers by means of spunbonding is based on the direct spinning of polymeric granulates into continuous filaments and subsequently manufacturing the fibrous layer.

Spunbond fabrics are produced by depositing extruded, spun fibers onto a moving belt in a uniform random manner followed by thermal bonding the fibers. The fibers are separated during the web laying process by air jets. Fiber bonds are generated by applying heated rolls or hot needles to partially melt the polymer and fuse the fibers together. Since molecular orientation increases the melting point, fibers that are not highly drawn can be used as thermal binding fibers. Polyethylene or random ethylene/propylene copolymers are used as low melting bonding sites.

Besides spunbonding, the technology of resin bonding also belongs to thermal bonding subjects. Using this technology to generate bonding sites, specific adhesives, based on e.g. epoxy, polyurethane and acrylic are added to the fibrous material and the resulting matrix is thermically treated. Thus the web is bonded with resin and/or thermal plastic resins dispersed within the fibrous material.

As a further thermal bonding technology through-air bonding involves the application of hot air to the surface of the fibrous fabric. The hot air is circulated just above the fibrous fabric, but does not push through the fibrous fabric. Bonding sites are generated by the addition of binders. Suitable binders used in through-air thermal bonding include crystalline binder fibers, bi-component binder fibers, and powders. When using crystalline binder fibers or powders, the binder melts entirely and forms molten droplets throughout the nonwoven's cross-section. Bonding occurs at these points upon cooling. In the case of sheath/core binder fibers, the sheath is the binder and the core is the carrier fiber. Products manufactured using through-air ovens tend to be bulky, open, soft, strong, extensible, breathable and absorbent. Through-air bonding followed by immediate cold calendering results in a thickness between a hot roll calendered product and one that has been though-air bonded without compression. Even after cold calendering, this product is softer, more flexible and more extensible than area-bond hot-calendered material.

Spunlacing (“hydroentanglement”) is a further method of increasing the integrity of a web. The formed web of loose fibers (usually air-laid or wet-laid) is first compacted and prewetted to eliminate air pockets. The technology of spunlacing uses multiple rows of fine high-speed jets of water to strike the web on a porous belt or moving perforated or patterned screen so that the fibers knot about one another. The water pressure generally increases from the first to the last injectors. Pressures as high as 150 bar are used to direct the water jets onto the web. This pressure is sufficient for most of the nonwoven fibers, although higher pressures are used in specialized applications.

The spunlace process is a nonwovens manufacturing system that employs jets of water to entangle fibers and thereby provide fabric integrity. Softness, drape, conformability, and relatively high strength are the major characteristics of spunlace nonwoven.

In newest researches benefits are found in some structural features of the resulting liquid-pervious layers. For example, the thickness of the layer is very important and influences together with its x-y dimension the acquisition-distribution behaviour of the layer. If there is further some profiled structure integrated, the acquisition-distribution behaviour can be directed depending on the three-dimensional structure of the layer. Thus 3D-polyethylene in the function of liquid-pervious layer is preferred.

Thus, suitable liquid-pervious sheets (A) (89) are nonwoven layers formed from the fibers above by thermal bonding, spunbonding, resin bonding or through-air bonding. Further suitable liquid-pervious layers are 3D-polyethylene layers and spunlace.

Preferably the 3D-polyethylene layers and spunlace show basis weights from 12 to 22 gsm.

Typically liquid-pervious sheets (A) (89) extend partially or wholly across the fluid-absorbent structure and can extend into and/or form part of all the preferred sideflaps, side wrapping elements, wings and ears.

Liquid-Impervious Sheet or Liquid Impervious Layer (B) (83)

The liquid-impervious sheet (B) (83) prevents the exudates absorbed and retained by the fluid-absorbent core from wetting articles which are in contact with the fluid-absorbent article, as for example bedsheets, pants, pajamas and undergarments. The liquid-impervious sheet (83) may thus comprise a woven or a nonwoven material, polymeric films such as thermoplastic film of polyethylene or polypropylene, or composite materials such as film-coated nonwoven material.

Suitable liquid-impervious sheets include nonwoven, plastics and/or laminates of plastic and nonwoven. Both, the plastics and/or laminates of plastic and nonwoven may appropriately be breathable, that is, the liquid-impervious layer (83) can permit vapors to escape from the fluid-absorbent material. Thus the liquid-impervious sheet has to have a definite water vapor transmission rate and at the same time the level of impermeability. To combine these features, suitable liquid-impervious layers (83) including at least two layers, e.g. laminates from fibrous nonwoven having a specified basis weight and pore size, and a continuous three-dimensional film of e.g. polyvinylalcohol as the second layer having a specified thickness and optionally having pore structure. Such laminates acting as a barrier and showing no liquid transport or wet through. Thus, suitable liquid-impervious layers (83) comprising at least a first breathable layer of a porous web which is a fibrous nonwoven, e.g. a composite web of a meltblown nonwoven layer or of a spunbonded nonwoven layer made from synthetic fibers and at least a second layer of a resilient three dimensional web consisting of a liquid-impervious polymeric film, e.g. plastics optionally having pores acting as capillaries, which are preferably not perpendicular to the plane of the film but are disposed at an angle of less than 90° relative to the plane of the film.

Suitable liquid-impervious sheets are permeable for vapor. Preferably the liquid-impervious sheet is constructed from vapor permeable material showing a water vapor transmission rate (WVTR) of at least about 100 gsm per 24 hours, preferably at least about 250 gsm per 24 hours and most preferred at least about 500 gsm per 24 hours.

Preferably the liquid-impervious sheet (B) (83) is made of nonwoven comprising hydrophobic materials, e.g. synthetic fibers or a liquid-impervious polymeric film comprising plastics e.g. polyethylene. The thickness of the liquid-impervious sheet is preferably 15 to 30 μm.

Further, the liquid-impervious sheet (B) (83) is preferably made of a laminate of nonwoven and plastics comprising a nonwoven having a density of 12 to 15 gsm and a polyethylene layer having a thickness of about 10 to 20 μm.

The typically liquid-impervious sheet (B) (83) extends partially or wholly across the fluid-absorbent structure and can extend into and/or form part of all the preferred sideflaps, side wrapping elements, wings and ears.

Fluid-Absorbent Core (C) (80)

The fluid-absorbent core (80) is disposed between the upper liquid-pervious sheet (A) (89) and the lower liquid-impervious sheet (B) (83).

According to the present invention the fluid-absorbent core (80) can be formed from an absorbent paper.

In order to increase the integrity of the fluid-absorbent core, the core may optionally provided with a cover (86) (e.g. tissue wrap). This cover may be at the top and/or at the bottom of the fluid-absorbent core (80) with bonding at lateral juncture and/or bonding at the distal juncture by hot-melt, ultrasonic bonding, thermal bonding or combination of bonding techniques know to persons skilled in the art. Further, this cover may include the whole fluid-absorbent core (80) with a unitary sheet of material and thus function as a wrap. Wrapping is possible as a full wrap, a partial wrap or as a C-Wrap.

The material of the core cover (86) may comprise any known type of substrate, including nonwovens, webs, garments, textiles, films, tissues and laminates of two or more substrates or webs. The core cover material may comprise natural fibers, such as cellulose, cotton, flax, linen, hemp, wool, silk, fur, hair and naturally occurring mineral fibers. The core cover material may also comprise synthetic fibers such as rayon and lyocell (derived from cellulose), polysaccharides (starch), polyolefin fibers (polypropylene, polyethylene), polyamides, polyester, butadiene-styrene block copolymers, polyurethane and combinations thereof. Preferably, the core cover comprises synthetic fibers or tissue.

The fibers may be mono- or multicomponent. Multicomponent fibers may comprise a homopolymer, a copolymer or blends thereof.

A schematic view of the absorbent paper/absorbent core (80) is shown in FIG. 17.

Absorbent paper (80) or absorbent core (80) respectively according to the invention comprises at least two layers of water-absorbent polymer particles one of which laid on top side (91) and another laid on the bottom (92). Both layers are connected (93) with e.g. adhesives, ultrasonic bonding and/or heat bonding on e.g. air-thru-bond nonwoven material (94) which is sandwiched by the two layers. For a good core integrity an upper tissue layer (95) and/or a lower tissue layer (96) are joined to the surface of the upper layer (91) and the lower layer (92) respectively.

The layers are preferably joined to each e.g. by addition of adhesives (93) or by mechanical, thermal or ultrasonic bonding or combinations thereof, whereas adhesives are preferred.

According to the invention the absorbent paper or absorbent core (80) respectively comprises at least two thin and flexible single layers of suitable absorbent material (91, 92). Each of these layers is macroscopically two-dimensional and planar and of very low thickness compared to the other dimensions. Said layer may incorporate superabsorbent material throughout the layer.

The layers may have different concentrations and different water-absorbent polymer material showing concentrations in the range from about 90 to 100%.

Furthermore it can be preferred that the water-absorbent polymer particles are placed within the core (80) in discrete regions, chambers or pockets, e.g. supported by at least an adhesive.

Techniques of application of the water-absorbent polymer materials into the absorbent core are known to persons skilled in the art and may be volumetric, loss-in-weight or gravimetric. Known techniques include the application by vibrating systems, single and multiple auger systems, dosing roll, weigh belt, fluid bed volumetric systems and gravitational sprinkle and/or spray systems. Further techniques of insertion are falling dosage systems consensus and contradictory pneumatic application or vacuum printing method of applying the fluid absorbent polymer materials.

The quantity of water-absorbent polymer particles within the fluid-absorbent core (absorbent paper) is from 100 to 500 gsm, preferably 200 to 400 gsm, more preferably 250 to 300 gsm in case of maxi diapers (size L),

wherein each layer contains at least 50 gsm water absorbent polymer particles preferably at least 100 gsm water absorbent polymer particles

The absorbent paper (80) may comprise also at least one layer of other material such as short-fiber air-laid nonwoven materials (94); nonwoven of materials such as polyethylene, polypropylene, nylon, polyester, and the like; cellulosic fibrous materials such as paper tissue or towels known in the art, wax-coated papers, corrugated paper materials, and the like; or fluff pulp. Said layer may also incorporate superabsorbent material throughout the layer. Said layer may further incorporate bi-component binding fibers.

The nonwoven (94) within in the core (80) is typically a single layer, e.g. made by air-thru bonded process. Its total basis weight is around 10 to 100 gsm, preferably 40 to 60

The absorbent core (80) comprises at least two core sheets or tissue layers (95, 96). The tissue layers are not restricted to tissue material such as paper it also refers to nonwovens. The material of the layer may comprise any known type of substrate, including webs, garments, textiles and films. The tissuelayer may comprise natural fibers, such as cellulose, cotton, flax, linen, hemp, wool, silk, fur, hair and naturally occurring mineral fibers. The tissue layer may also comprise synthetic fibers such as rayon and lyocell (derived from cellulose), polysaccharides (starch), polyolefin fibers (polypropylene, polyethylene), polyamides, polyester, butadiene-styrene block copolymers, polyurethane and combinations thereof. Preferably, the tissue layer comprises cellulose fibers. It is preferred that the tissue layer is made from ca. 50% wood pulp and 50% chemical viscose fibers at >45 gsm to provide tensile strength and integrity.

According to the invention the upper and lower tissue layers (95, 96) each total basis weight is from 10 to 100 gsm, preferably 30 to 80 gsm.

According to the invention it is preferred that the fluid-absorbent core (80) comprises not more than 20% by weight of an adhesive, preferably not more than 10% by weight of an adhesive. Preferably the adhesive is a hotmelt adhesive.

The absorbent paper (80) has a total basis weight ranging from about 150 gsm to about 2000 gsm, preferably from about 300 gsm to about 750 gsm, and more preferrably from about 500 gsm to about 650 gsm.

According to the invention the at least two layers (91), (92) containing each at least one kind of water-absorbent polymer particles.

The water absorbent polymer particles in each layer (91, 92) may be different.

It may be also preferred that at least one layer (91 or 92) contains a blend of water absorbent polymer particles

It is preferred that the upper layer (91) facing the upper liquid permeable sheet (topsheet) (89) contains surface-postcrosslinked water-absorbent polymer particles with a sphericity of at least 0.89.

Preferably the CRC of the polymer particles in the upper layer (91) facing the upper liquid permeable sheet (89) is at least 34 g/g. Preferably the CRC is at least 36 g/g and more preferably 38 g/g.

Preferably the AUL (21 g cm⁻²) of the polymer particles in the upper layer (91) facing the upper liquid permeable sheet (89) is at least 30 g/g. Preferably the AUL is at least 32 g/g and more preferably 34 g/g

It is particular advantageous that the surface-postcrosslinked water-absorbent polymer particles exhibit a very high centrifuge retention capacity (CRC) and a high absorption under load (AUL, 21 g/cm²), and that the sum of these parameters (=CRC+AUL(21 g/cm⁻²)) is at least 65 g/g, preferably at least 70 g/g, most preferably at least 75 g/g,

As the centrifuge retention capacity (CRC) is the maximum liquid retention capacity of the surface-postcrosslinked water-absorbent polymer particles it is of interest to maximize this parameter. However the absorption under load (AUL) is important to allow in a hygiene article further liquid to pass easily through the article structure to enable rapid uptake of this liquid.

According to a further object of the invention it is preferred that also the water-absorbent polymer particles of the lower layer (92) have a sphericity of 0.89.

According to the invention the water-absorbent polymer particles at least in the upper layer (91) facing the upper liquid permeable sheet (89) are surface-postcrosslinked.

In one embodiment of the inventive absorbent paper the upper layer (91) comprises 100% by weight of water-absorbent particles and/or the lower layer (92) comprises 100% by weight of water-absorbent particles.

According to the invention a preferred absorbent paper (80) comprises top and bottom layers (91, 92) of water-absorbing polymer particles containing each 130 grams per square meter (g/m²). Both layers are glued (93) with 0.5 g/m² hot melt adhesive on 50 g/m² air-thru-bond nonwoven material (94) and are then sandwiched with two layers of 45 g/m² condensed tissue layers on the top (95) and bottom (96) using hot-melt glue applied to the surface at 2.0 g/m². Total hot-melt glue used is 2.5 g/m² for both top and bottom layers.

The density of the fluid-absorbent core is in the range of 0.1 to 0.25 g/cm³, preferably 0.1 to 0.28 g/cm³. The thickness of the fluid-absorbent core is in the case of diapers in the range of 1 to 8 mm, preferably 1 to 5 mm, more preferably 1.5 to 3 mm, in the case of adult-incontinence products in the range of 3 to 15 mm.

FIG. 18 illustrates a possible production process for an absorbent core (80).

A first water-absorbent polymer (230) is dropped onto one side of a nonwoven material (250). Then an adhesive (200) is applied to the top tissue paper (210). The tissue paper (210) then is laminated with the side of the nonwoven (250) carrying the water-absorbent polymer (230). Afterwards the nonwoven (250) is turned around and the second water-absorbent polymer (240) is dropped onto the other side of the nonwoven (250). An adhesive (200) is applied to the bottom or lower tissue paper (260). The tissue paper (260) then is laminated with the side of the nonwoven (250) carrying the water-absorbent polymer (240). Finally the absorbent paper is slit to the desired width and winding.

The fluid-absorbent core (80) typically has a uniform size or profile. Suitable fluid-absorbent cores can also have profiled structures, concerning the shape of the core and/or the content of water-absorbent polymer particles and/or the distribution of the water-absorbent polymer particles and/or the dimensions of the different layers if a layered fluid-absorbent core is present.

The shape of the core (80) in view from above (x-y dimension) can be rectangular, anatomical shaped with a narrower crotch area or any other shapes.

The top view area of the fluid-absorbent core (C) (80) is preferably at least 200 cm², more preferably at least 250 cm², most preferably at least 300 cm². The top view area is the part of the core that is face-to-face to the upper liquid-pervious layer.

The fluid-absorbent core (80) may comprise additional additives typically present in fluid-absorbent articles known in the art. Exemplary additives are fibers for reinforcing and stabilizing the fluid-absorbent core. Preferably polyethylene is used for reinforcing the fluid-absorbent core.

Further suitable stabilizer for reinforcing the fluid-absorbent core are materials acting as binder.

In varying the kind of binder material or the amount of binder used in different regions of the fluid-absorbent core it is possible to get a profiled stabilization. For example, different binder materials exhibiting different melting temperatures may be used in regions of the fluid-absorbent core, e.g. the lower melting one in the central region of the core, and the higher melting in the distal regions. Suitable binder materials may be adhesive or non-adhesive fibers, continuously or discontinuously extruded fibers, bi-component staple fibers, nonelastomeric fibers and sprayed liquid binder or any combination of these binder materials.

Further, thermoplastic compositions usually are added to increase the integrity of the core layer. Thermoplastic compositions may comprise a single type of thermoplastic polymers or a blend of thermoplastic polymers. Alternatively, the thermoplastic composition may comprise hot melt adhesives comprising at least one thermoplastic polymer together with thermoplastic diluents such as tackifiers, plasticizers or other additives, e.g. antioxidants. The thermoplastic composition may further comprise pressure sensitive hot melt adhesives comprising e.g. crystalline polypropylene and an amorphous polyalphaolefin or styrene block copolymer and mixture of waxes.

Concerning odor control, perfumes and/or odor control additives are optionally added. Suitable odor control additives are all substances of reducing odor developed in carrying fluid-absorbent articles over time known in the art. Thus, suitable odor control additives are inorganic materials, such as zeolites, activated carbon, bentonite, silica, aerosile, kieselguhr, clay; chelants such as ethylenediamine tetraacetic acid (EDTA), cyclodextrins, aminopolycarbonic acids, ethylenediamine tetramethylene phosphonic acid, aminophosphate, polyfunctional aromates, N,N-disuccinic acid. Suitable odor control additives are further antimicrobial agents.

Suitable odor control additives are further compounds with anhydride groups such as maleic-, itaconic-, polymaleic- or polyitaconic anhydride, copolymers of maleic acid with C₂-C₈ olefins or styrene, polymaleic anhydride or copolymers of maleic anhydride with isobutene, di-isobutene or styrene, compounds with acid groups such as ascorbic, benzoic, citric, salicylic or sorbic acid and fluid-soluble polymers of monomers with acid groups, homo- or copolymers of C₃-C₅ mono-unsaturated carboxylic acids.

Newest developments propose the addition of wetness indication additives.

Suitable wetness indication additives comprising a mixture of sorbitan monooleate and polyethoxylated hydrogenated castor oil. Preferably, the amount of the wetness indication additive is in the range of about 0.0001 to 2% by weight related to the weight of the fluid-absorbent core.

Optional Acquisition-Distribution Layer (D)

An optional acquisition-distribution layer (D) is located between the upper layer (A) (89) and the fluid-absorbent core (C)(80) and is preferably constructed to efficiently acquire discharged body fluids and to transfer and distribute them to other regions of the fluid-absorbent composition or to other layers, where the body fluids are immobilized and stored. Thus, the upper layer transfers the discharged liquid to the acquisition-distribution layer (D) for distributing it to the fluid-absorbent core.

The acquisition-distribution layer comprises fibrous material and optionally water-absorbent polymer particles.

The fibrous material may be hydrophilic, hydrophobic or can be a combination of both hydrophilic and hydrophobic fibers. It may be derived from natural fibers, synthetic fibers or a combination of both.

Suitable acquisition-distribution layers are formed from cellulosic fibers and/or modified cellulosic fibers and/or synthetics or combinations thereof. Thus, suitable acquisition-distribution layers may contain cellulosic fibers, in particular wood pulp fluff. Examples of further suitable hydrophilic, hydrophobic fibers, as well as modified or unmodified natural fibers are given in the chapter “Liquid-pervious sheet or liquid pervious layer (89)” above.

Especially for providing both fluid acquisition and distribution properties, the use of modified cellulosic fibers is preferred. Examples for modified cellulosic fibers are chemically treated cellulosic fibers, especially chemically stiffened cellulosic fibers. The term “chemically stiffened cellulosic fibers” means cellulosic fibers that have been stiffened by chemical means to increase the stiffness of the fibers. Such means include the addition of chemical stiffening agent in the form of surface coatings, surface cross-linking and impregnates. Suitable polymeric stiffening agents can include: cationic modified starches having nitrogen-containing groups, latexes, wet strength resins such as polyamide-epichlorohydrin resin, polyacrylamide, urea formaldehyde and melamine formaldehyde resins and polyethylenimine resins.

Stiffening may also include altering the chemical structure, e.g. by crosslinking polymer chains. Thus crosslinking agents can be applied to the fibers that are caused to chemically form intrafiber crosslink bonds. Further cellulosic fibers may be stiffened by crosslink bonds in individualized form. Suitable chemical stiffening agents are typically monomeric crosslinking agents including C₂-C₈ dialdehyde, C₂-C₈ monoaldehyde having an acid functionality, and especially C₂-C₉ polycarboxylic acids.

Preferably the modified cellulosic fibers are chemically treated cellulosic fibers. Especially preferred are curly fibers which can be obtained by treating cellulosic fibers with citric acid. Preferably the basis weight of cellulosic fibers and modified cellulosic fibers is from 50 to 200 gsm.

Suitable acquisition-distribution layers further include synthetic fibers. Known examples of synthetic fibers are found in the Chapter “Liquid-pervious sheet or liquid pervious layer (89)” above. Another possibility available is 3D-polyethylene film with dual function as a liquid-pervious layer (A) (89) and acquisition-distribution layer.

Further, as in the case of cellulosic fibers, hydrophilic synthetic fibers are preferred. Hydrophilic synthetic fibers may be obtained by chemical modification of hydrophobic fibers. Preferably, hydrophilization is carried out by surfactant treatment of hydrophobic fibers. Thus the surface of the hydrophobic fiber can be rendered hydrophilic by treatment with a nonionic or ionic surfactant, e.g., by spraying the fiber with a surfactant or by dipping the fiber into a surfactant. Further preferred are permanent hydrophilic synthetic fibers. The fibrous material of the acquisition-distribution layer may be fixed to increase the strength and the integrity of the layer. Technologies for consolidating fibers in a web are mechanical bonding, thermal bonding and chemical bonding. Detailed description of the different methods of increasing the integrity of the web is given in the Chapter “Liquid-pervious sheet or liquid pervious layer (89)” above.

Preferred acquisition-distribution layers comprise fibrous material and water-absorbent polymer particles distributed within. The water-absorbent polymer particles may be added during the process of forming the layer from loose fibers, or, alternatively, it is possible to add monomer solution after the formation of the layer and polymerize the coating solution by means of UV-induced polymerisation technologies. Thus, “in situ”-polymerisation is a further method for the application of water-absorbent polymers.

Thus, suitable acquisition-distribution layers comprising from 80 to 100% by weight a fibrous material and from 0 to 20% by weight water-absorbent polymer particles; preferably from 85 to 99.9% by weight a fibrous material and from 0.1 to 15% by weight water-absorbent polymer particles; more preferably from 90 to 99.5% by weight a fibrous material and from 0.5 to 10% by weight water-absorbent polymer particles; and most preferably from 95 to 99% by weight a fibrous material and from 1 to 5% by weight water-absorbent polymer particles.

Preferred acquisition-distribution layers show basis weights in the range from 20 to 200 gsm, most preferred in the range from 40 to 60 gsm, depending on the concentration of water-absorbent polymer particles.

Alternatively a liquid-impervious layer (D) comprising a synthetic resin film between (A) (89) and (C) (80) acting as an distribution layer and quickly transporting the supplied urine along the surface to the upper lateral portion of the fluid-absorbent core (C)(80). Preferably, the upper liquid-impervious layer (D) is smaller than the under-laying fluid-absorbent core (C) (80). There is no limit in particular to the material of the liquid-impervious layer (D). Such a film made of a resin such as polyethylene, polypropylene, polyethylene terephthalate, polyurethane, or crosslinked polyvinyl alcohol and an air-permeable, but liquid-impervious, so-called: “breathable” film made of above described resin, may be used.

Preferably, the upper liquid-impervious layer (D) comprises a porous polyethylene film for both quickly acquisition and distribution of fluid.

Alternatively a bundle of synthetic fibers acting as acquisition-distribution layer loosely distributed on top of the fluid-absorbent core may be used. Suitable synthetic fibers are of copolyester, polyamide, copolyamide, polylactic acid, polypropylene or polyethylene, viscose or blends thereof. Further bicomponent fibers can be used. The synthetic fiber component may be composed of either a single fiber type with a circular cross-section or a blend of two fibre types with different cross-sectional shapes. Synthetic fibers arranged in that way ensuring a very fast liquid transport and canalisation. Preferrably bundles of polyethylene fibers are used.

Other Optional Components (E) 1. Leg Cuff

Typical leg cuffs comprising nonwoven materials which can be formed by direct extrusion processes during which the fibers and the nonwoven materials are formed at the same time, or by laying processes of preformed fibers which can be laid into nonwoven materials at a later point of time. Examples for direct extrusion processes include spunbonding, meltblowing, solvent spinning, electrospinning and combinations thereof. Examples of laying processes include wet-laying and dry-laying (e.g. air-laying, carding) methods. Combinations of the processes above include spunbond-meltblown-spunbond (sms), spunbond-meltblow-meltblown-spunbond (smms), spunbond-carded (sc), spunbond-airlaid (sa), meltblown-airlaid (ma) and combinations thereof. The combinations including direct extrusion can be combined at the same point in time or at a subsequent point in time. In the examples above, one or more individual layers can be produced by each process. Thus, “sms” means a three layer nonwoven material, “smsms” or “ssmms” means a five layer nonwoven material. Usually, small type letters (sms) designate individual layers, whereas capital letters (SMS) designate the compilation of similar adjacent layers.

Further, suitable leg cuffs are provided with elastic strands.

Preferred are leg cuffs from synthetic fibers showing the layer combinations sms, smms or smsms. Preferred are nonwovens with the density of 13 to 17 gsm. Preferably leg cuffs are provided with two elastic strands.

2. Elastics

The elastics are used for securely holding and flexibly closing the fluid-absorbent article around the wearers' body, e.g. the waist and the legs to improve containment and fit. Leg elastics are placed between the outer and inner layers or the fluid-absorbent article, or between the outer garment facing cover and the user facing bodyside liner. Suitable elastics comprising sheets, ribbons or strands of thermoplastic polyurethane, elastomeric materials, poly(ether-amide) block copolymers, thermoplastic rubbers, styrene-butadiene copolymers, silicon rubbers, natural rubbers, synthetic rubbers, styrene isoprene copolymers, styrene ethylene butylene copolymers, nylon copolymers, spandex fibers comprising segmented polyurethane and/or ethylene-vinyl acetate copolymer. The elastics may be secured to a substrate after being stretched, or secured to a stretched substrate. Otherwise, the elastics may be secured to a substrate and then elasticized or shrunk, e.g. by the application of heat.

3. Closing System

The closing system can include tape tabs, landing zone, elastomerics, pull ups and the belt system or combinations thereof

At least a part of the first waist region is attached to a part of the second waist region by the closing system to hold the fluid-absorbent article in place and to form leg openings and the waist of the fluid-absorbent article. Preferably the fluid-absorbent article is provided with a re-closable closing system.

The closing system is either re-sealable or permanent, including any material suitable for such a use, e.g. plastics, elastics, films, foams, nonwoven substrates, woven substrates, paper, tissue, laminates, fiber reinforced plastics and the like, or combinations thereof. Preferably the closing system includes flexible materials and works smooth and softly without irritating the wearer's skin.

One part of the closing elements is an adhesive tape, or comprises a pair of laterally extending tabs disposed on the lateral edges of the first waist region. Tape tabs are typically attached to the front body panel and extend laterally from each corner of the first waistband. These tape tabs include an adhesive inwardly facing surface which is typically protected prior to use by a thin, removable cover sheet.

Suitable tape tabs may be formed of thermoplastic polymers such as polyethylene, polyurethane, polystyrene, polycarbonate, polyester, ethylene vinyl acetate, ethylene vinyl alcohol, ethylene vinyl acetate acrylate or ethylene acrylic acid copolymers.

Suitable closing systems comprise further a hook portion of a hook and loop fastener and the target devices comprise the loop portion of a hook and loop fastener.

Suitable mechanical closing systems including a landing zone. Mechanical closing systems may fasten directly into the outer cover. The landing zone may act as an area of the fluid-absorbent article into which it is desirable to engage the tape tabs. The landing zone may include a base material and a plurality of tape tabs. The tape tabs may be embedded in the base material of the landing zone. The base material may include a loop material. The loop material may include a backing material and a layer of a nonwoven spunbond web attached to the backing material.

Thus suitable landing zones can be made by spunbonding. Spunbonded nonwoven are made from melt-spun fibers formed by extruding molten thermoplastic material. Preferred is bi-oriented polypropylene (BOPP), or brushed/closed loop in the case of mechanical closing systems.

Further, suitable mechanical closing systems including elasticomeric units serving as a flexible abdominal and/or dorsal discrete waist band, flexible abdomen and/or dorsal zones located at distal edge for fluid-absorbents articles, such as pants or pull-ups. The elasticomeric units enable the fluid-absorbent article to be pulled down by the wearer as e.g. a training pant.

Suitable pants-shaped fluid-absorbent article has front abdominal section, rear dorsal section, crotch section, side sections for connecting the front and rear sections in lateral direction, hip section, elastic waist region and liquid-tight outer layer. The hip section is arranged around the waist of the user. The disposable pants-shaped fluid-absorbent article (pull-up) has favorable flexibility, stretchability, leak-proof property and fit property, hence imparts excellent comfort to the wearer and offers improved mobility and discretion.

Suitable pull-ups comprising thermoplastic films, sheets and laminates having a low modulus, good tear strength and high elastic recovery.

Suitable closing systems may further comprise elastomerics for the production of elastic areas within the fastening devices of the fluid-absorbent article. Elastomerics provide a conformable fit of the fluid-absorbent article to the wearer at the waist and leg openings, while maintaining adequate performance against leakage.

Suitable elastomerics are elastomeric polymers or elastic adhesive materials showing vapor permeability and liquid barrier properties. Preferred elastomerics are retractable after elongation to a length equivalent to its original length.

Suitable closing systems further comprise a belt system, comprising waist-belt and leg-belts for flexibly securing the fluid-absorbent article on the body of the wearer and to provide an improved fit on the wearer. Suitable waist-belts comprising two elastic belts, a left elastic belt, and a right elastic belt. The left elastic belt is associated with each of the left angular edges. The right elastic belt associated with each of the right angular edges. The left and right side belts are elastically extended when the absorbent garment is laid flat. Each belt is connected to and extends between the front and rear of the fluid-absorbent article to form a waist hole and leg holes.

Preferably the belt system is made of elastomerics, thus providing a conformable fit of the fluid-absorbent article and maintaining adequate performance against leakage.

Preferred closing systems are so-called “elastic ears” attached with one side of the ear to the longitudinal side edges located at the rear dorsal longitudinal edge of the chassis of the fluid-absorbent article. Commercially available fluid-absorbent articles include stretchable ears or side panels which are made from a stretchable laminate e.g. nonwoven webs made of mono- or bi-component fibers. Especially preferred closing systems are stretchable laminates comprising a core of several layers each of different fibrous materials, e.g. meltblown fibers, spunbond fibers, containing multicomponent fibers having a core comprising a first polymer having a first melt temperature and a sheath comprising a second polymer having a second melt temperature; and a web of an elastomeric material as top and bottom surfaces to form said laminate.

D. Fluid-Absorbent Article Construction

The present invention further relates to the joining of the components and layers, films, sheets, tissues or substrates mentioned above to provide the fluid-absorbent article. At least two, preferably all layers, films, sheets, tissues or substrates are joined.

Suitable fluid-absorbent articles include a single- or multiple fluid-absorbent core-system.

Preferably fluid-absorbent articles include a single- or double fluid-absorbent core-system.

Suitable fluid-storage layers of the fluid-absorbent core (80) comprising 0 to 10% by weight fibrous material and from 90 to 100% by weight a water-absorbent polymer material. In case of fibrous material present the fibrous materials homogeneously or in-homogeneously mixed with water-absorbent polymer particles. Suitable fluid-storage layers of the fluid-absorbent core including a layered fluid-absorbent core-system comprising 100% by weight of water-absorbent polymer material or homogeneous or in-homogeneous mixtures of fibrous materials and water-absorbent polymer particles.

In order to immobilize the water-absorbent polymer particles, the adjacent layers are fixed by the means of thermoplastic materials, thereby building connections throughout the whole surface or alternatively in discrete areas of junction. For the latter case, cavities or pockets are built carrying the water-absorbent particles. The areas of junction may have a regular or irregular pattern, e.g. aligned with the longitudinal axis of the fluid-absorbent core or in a pattern of polygons, e.g. pentagons or hexagons. The areas of junction itself may be of rectangular, circular or squared shape with diameters between about 0.5 mm and 2 mm. Fluid-absorbent articles comprising areas of junction show a better wet strength.

The construction of the products chassis and the components contained therein is made and controlled by the discrete application of hotmelt adhesives as known to people skilled in the art. Examples would be e.g. Dispomelt 505B, Dispomelt Cool 1101, as well as other specific function adhesives manufactured by Bostik, Henkel or Fuller.

In order to ensure wicking of applied body fluids, preferred fluid-absorbent article show channels for better transport. Channels are formed by compressional forces of e.g. the top sheet against the fluid-absorbent core. Compressive forces may be applied e.g. by heat-treatment between two heated calendar rollers. As an effect of compression both on top sheet and fluid-absorbent core deform such that a channel is created. Body fluids are flowing along this channel to places where they are absorbed and leakage is prevented. Otherwise, compression leads to higher density; this is the second effect of the channel to canalize insulted fluids. Additionally, compressive forces on diaper construction improve the structural integrity of the fluid-absorbent article.

Typically fluid-absorbent articles comprising at least an upper liquid-pervious layer (89), at least a lower liquid-impervious layer (83) and at least one fluid-absorbent core (80) between the layer (89) and the layer (83) besides other optional layers.

The inventive fluid-absorbent article shows improved rewet and fluid acquisition properties.

A fluid absorbent article according to the invention comprising

-   -   (A) an upper liquid-pervious sheet (89),     -   (B) a lower liquid-impervious sheet (83),     -   (C) a fluid-absorbent core between the upper sheet (89) and the         lower sheet (83), comprising at least two layers comprising         water-absorbent polymer particles, an upper layer (91) and a         lower layer (92), each layer comprising from 0 to 10% by weight         fibrous material and from 90 to 100% by weight water-absorbent         polymer particles, based on the sum of water-absorbent polymer         particles and fibrous material;     -   (D) an optional acquisition-distribution layer (D) between (89)         and (80),     -   (F) other optional components,     -   wherein the water absorbent polymer particles within the upper         layer have a sphericity of at least 0.89 and a CRC of at least         34 g/g.

An inventive fluid absorbent article furthermore comprises

a fluid-absorbent core between (89) and (83) comprising an upper and a lower tissue layer (95, 96), an upper layer (91) comprising water-absorbent polymer particles and a lower layer (92), comprising water-absorbent polymer particles, a nonwoven material (94), sandwiched between the upper layer (91) and lower layer (92) wherein the layers are connected by adhesives, ultrasonic bonding and/or heat bonding.

Furthermore the AUL ((0.3 psi, 21 g cm⁻², EDANA 442.2-02) for the water absorbent polymer particles of the upper layer (91) is at least 30 g/g.

It is also preferred that the water absorbent polymer particles within the upper layer (91) have a sphericity of at least 0.89 and the sum of the CRC and AUL ((0.3 psi, 21 g cm⁻², EDANA 442.2-02) of the water absorbent polymer particles is at least 65 g/g.

Especially the properties of the water-absorbent particles within the upper layer have a great impact on the features of the absorbent core and total absorbent article respectively.

According to the invention the upper layer (91) and or the lower layer (92) comprises at least 90, preferably 95%, more preferably 100% by weight of water-absorbent particles.

As it is preferred that the layers containing water-absorbent polymer show different properties to better adjust the properties of the fluid-absorbent articles the water absorbent polymer particles in each layer are different.

In order to increase the control of body fluid absorption it may be advantageous to add one or more further fluid-absorbent cores. The addition of a second fluid-absorbent core to the first fluid-absorbent core offers more possibilities in body fluid transfer and distribution. Moreover higher quantities of discharged body fluids can be retained. Having the opportunity of combining several layers showing different water-absorbent polymer concentration and content, it is possible to reduce the thickness of the fluid-absorbent article to a minimum even if there are several fluid-absorbent cores included.

Methods:

The measurements should, unless stated otherwise, be carried out at an ambient temperature of 23±2° C. and a relative atmospheric humidity of 50±10%. The water-absorbent polymers are mixed thoroughly before the measurement.

The “WSP” standard test methods are described in: “Standard Test Methods for the Nonwovens Industry”, jointly issued by the “Worldwide Strategic Partners” EDANA (European Disposables and Nonwovens Association, Avenue Eugene Plasky, 157, 1030 Brussels, Belgium, www.edana.org) and INDA (Association of the Nonwoven Fabrics Industry, 1100 Crescent Green, Suite 115, Cary, N.C. 27518, U.S.A., www.inda.org). This publication is available both from EDANA and INDA.

Accelerated Aging Test

Measurement 1 (Initial color): A plastic dish with an inner diameter of 9 cm is overfilled with superabsorbent polymer particles. The surface is flattened at the height of the petri dish lip by means of a knife and the CIE color values and the HC 60 value are determined.

Measurement 2 (after aging): A plastic dish with an inner diameter of 9 cm is overfilled with superabsorbent polymer particles. The surface is flattened at the height of the petri dish lip by means of a knife. The plastic dish (without a cover) is then placed in a humidity chamber at 60° C. and a relative humidity of 86%. The plastic dish is removed from the humidity chamber after 7, 14, and 21 days, cooled down to room temperature and the CIE color values are determined.

Absorbency Under No Load (AUNL)

The absorbency under no load of the water-absorbent polymer particles is determined analogously to the EDANA recommended test method No. WSP 242.3 (11) “Gravimetric Determination of Absorption Under Pressure”, except using a weight of 0.0 g/cm² instead of a weight of 21.0 g/cm².

Absorbency Under Load (AUL)

The absorbency under load of the water-absorbent polymer particles is determined by the EDANA recommended test method No. WSP 242.3 (11) “Gravimetric Determination of Absorption Under Pressure”

Absorbency Under High Load (AUHL)

The absorbency under high load of the water-absorbent polymer particles is determined analogously to the EDANA recommended test method No. WSP 242.3 (11) “Gravimetric Determination of Absorption Under Pressure”, except using a weight of 49.2 g/cm² instead of a weight of 21.0 g/cm².

Bulk Density

The bulk density of the water-absorbent polymer particles is determined by the EDANA recommended test method No. WSP 250.3 (11) “Gravimetric Determination of Density”.

Basis Weight

The basis weight is determined at discrete regions of the fluid-absorbent core: the front overall average; the insult zone and the back overall average.

The article nonwoven face is pinned upwards onto the inspection table. Then an insult point is marked on the fluid-absorbent article. The insult point is marked on the article accordingly with regard to the type and gender of the diaper to be tested (i.e. in the centre of the fluid-absorbent core for girl, 2.5 cm towards the front for unisex and 5 cm towards the front for boy).

Then lines for the following zones are marked on the fluid-absorbent article in dependence of the diaper to be tested, e. g. for boy diapers:

-   -   for the front overall average zone 5.5 cm forward of the center         of the core to the front distal edge of the core;     -   for the insult zone 5.5 cm forward and 0.5 cm backwards of the         center of the core;     -   for the back overall average zone 0.5 cm backward of the center         of the core to the rear distal edge of the core

The length (ZL) and width (ZW) of each zone is recorded. Then the previously marked zones are cut out and the record weight (ZWT) of each zone is taken.

Before calculating the basis weight, the area of each zone must first be calculated as follows:

Zonal Area (ZA)=(ZW×ZL) [cm²]

The Zonal Basis Weight (ZBW) is then calculated as follows:

Zonal Basis Weight (ZBW)=ZWT/(ZW*ZL)*10000 [g/m²]

For example, if ZW is 6 cm, ZL is 10 cm and ZWT is 4.5 g the Zonal Basis Weight (ZBW) is:

ZBW=4.5 g/(6 cm×10 cm)*10000=750 gsm

Conversion of Gram per Square Centimeter g/cm² to Gram per Square Meter g/m²:

10 000×g/cm²=g/m²

Conversion of Gram per Square Meter g/m² to Gram per Square Centimeter g/cm²:

0.0001×g/m²=g/cm²

Centrifuge Retention Capacity (CRC) (EDANA 441.2-02)

The centrifuge retention capacity of the water-absorbent polymer particles is determined by the EDANA recommended test method No. WSP 241.3 (11) “Fluid Retention Capacity in Saline, After Centrifugation”, wherein for higher values of the centrifuge retention capacity larger tea bags have to be used.

Color Value (CIE Color Numbers [L, a, b])

Measurement of the color value is done by means of a colorimeter model, LabScan XE S/N LX17309″ (HunterLab; Reston; U.S.A.) according to the CIELAB procedure (Hunterlab, Volume 8, 1996, Issue 7, pages 1 to 4). Colors are described by the coordinates L, a, and b of a three-dimensional system. L characterizes the brightness, whereby L=0 is black and L=100 is white. The values for a and b describe the position of the color on the color axis red/green resp. yellow/blue, whereby positive a values stand for red colors, negative a values for green colors, positive b values for yellow colors, and negative b values for blue colors.

The measurement of the color value is in agreement with the tristimulus method according to DIN 5033-6.

Extractables

The level of extractable constituents in the water-absorbent polymer particles is determined by the EDANA recommended test method No. WSP 270.3 (11) “Extractables”.

Free Swell Rate (FSR)

1.00 g (=W1) of the dry water-absorbent polymer particles is weighed into a 25 ml glass beaker and is uniformly distributed on the base of the glass beaker. 20 ml of a 0.9% by weight sodium chloride solution are then dispensed into a second glass beaker, the content of this beaker is rapidly added to the first beaker and a stopwatch is started. As soon as the last drop of salt solution is absorbed, confirmed by the disappearance of the reflection on the liquid surface, the stopwatch is stopped. The exact amount of liquid poured from the second beaker and absorbed by the polymer in the first beaker is accurately determined by weighing back the second beaker (=W2). The time needed for the absorption, which was measured with the stopwatch, is denoted t. The disappearance of the last drop of liquid on the surface is defined as time t.

The free swell rate (FSR) is calculated as follows:

FSR [g/gs]=W2/(W1×t)

When the moisture content of the hydrogel-forming polymer is more than 3% by weight, however, the weight W1 must be corrected for this moisture content.

Free Swell Capacity (FSC)

The free swell capacity of the water-absorbent polymer particles is determined by the EDANA recommended test method No. WSP 240.3 (11) “Free Swell Capacity in Saline, Gravimetric Determination”, wherein for higher values of the free swell capacity larger tea bags have to be used.

Mean Sphericity

The mean sphericity is determined with the Camziser® image analysis system (Retsch Technology GmbH; Haan; Germany) using the particle diameter fraction from 100 to 1,000 μm.

Moisture Content

The moisture content of the water-absorbent polymer particles is determined by the EDANA recommended test method No. WSP 230.3 (11) “Mass Loss Upon Heating”.

Particle Size Distribution

The particle size distribution of the water-absorbent polymer particles is determined by the EDANA recommended test method No. WSP 220.3 (11) “Particle Size Distribution”.

The average particle diameter (d₅₀) here is the value of the mesh size which gives rise to a cumulative 50% by weight.

The degree of polydispersity a of the particle size particle is calculated by

α=(d _(84.13) −d _(15.87))/(2×d ₅₀)

wherein d_(15.87) and d_(84.13) is the value of the mesh size which gives rise to a cumulative 15.87% respective 84.13% by weight.

Quick Dryness Test

The test specimen is opened and laid flat on testing bench. Measure 150 mL of 0.9% saline solution using 200 mL glass beaker. Pour the saline solution into the separatory funnel using the pouring glass funnel. The separatory funnel shall be controlled flow rate at 20 mL/sec. Pour the saline solution through the separatory funnel at the center of test specimen, once the water first contact the specimen, simultaneously start a stopwatch. Allow the water to drain out from the separatory funnel and allow the saline solution to be absorbed into the specimen for 2.5 minutes. Prepare 30-40 pieces of filter paper (MN 615, OD 9 cm) and record its dry weight in grams (DW₂). After 2.5 minutes, place the filter paper on to the test specimen at the center and place 2.5 kgs circular weight with OD 8 cm (Picture 1) on top the filter paper. Wait for 30 seconds monitored by a timer, then take out the weight and the filter paper. Weigh the filter and record its wet weight in grams (WW₂).

Quick Dryness (g)=WW ₂ (g)−DW ₂ (g)

Residual Monomers

The level of residual monomers in the water-absorbent polymer particles is determined by the EDANA recommended test method No. WSP 210.3-(11) “Residual Monomers”.

Saline Flow Conductivity (SFC)

The saline flow conductivity is, as described in EP 0 640 330 A1, determined as the gel layer permeability of a swollen gel layer of water-absorbent polymer particles, although the apparatus described on page 19 and in FIG. 8 in the aforementioned patent application was modified to the effect that the glass frit (40) is no longer used, the plunger (39) consists of the same polymer material as the cylinder (37) and now comprises 21 bores having a diameter of 9.65 mm each distributed uniformly over the entire contact surface. The procedure and the evaluation of the measurement remains unchanged from EP 0 640 330 A1. The flow rate is recorded automatically.

The saline flow conductivity (SFC) is calculated as follows:

SFC [cm³s/g]=(Fg(t=0)×L0)/(d×A×WP),

where Fg(t=0) is the flow rate of NaCl solution in g/s, which is obtained by means of a linear regression analysis of the Fg(t) data of the flow determinations by extrapolation to t=0, L0 is the thickness of the gel layer in cm, d is the density of the NaCl solution in g/cm³, A is the surface area of the gel layer in cm² and WP is the hydrostatic pressure over the gel layer in dyn/cm².

Strike-Thru Time and Rewet (Chinese Standard)

The test specimen is opened and freely stand on the testing bench. Measure 80 mL of 0.9% saline solution using 100 mL measuring cylinder. Pour the saline solution into the separatory funnel (Picture 1). The separatory funnel shall be controlled flow rate at 20 mL/sec. Pour the water through the separatory funnel at the center of test specimen, once the water first contact the specimen, simultaneously start a stopwatch. Allow the water to drain out from the separatory funnel and visually observe the saline solution being absorbed by the specimen. Once the top surface of the test specimen turn white, stop the stopwatch and record the first “strike-thru time” in seconds. Allow the test specimen to fully absorb the saline for 5 minutes, monitored by a count-down timer. After 5 minutes, insult another 80 mL 0.9% saline solution at the center of the test specimen using the separatory funnel. Record the second “strike-thru time” after the saline solution is fully absorbed into the test specimen (visually observe by first white on the top surface). Allow the specimen to absorb the saline solution for 5 minutes using a count-down timer. Prepare 30-40 pieces of filter paper (MN 615, OD 11 cm) and record its dry weight in grams (DW₃). After 5 minutes, place the filter paper on to the test specimen at the center and place 1.2 kgs circular weight with OD 10 cm (giving a pressure of 0.22 psi) on top the filter paper. Wait for 1 minute monitored by a timer, then take out the weight and the filter paper. Weigh the filter and record its wet weight in grams (WW₃).

Rewet (g)=WW ₃ (g)−DW ₃ (g)

Water Pouring Time and Rewet Test

This test consists of multiple insults of deionized water. The rewet is measured by the amount of fluid the article released under pressure. The rewet is measured after each insult.

The test specimen (fluid-absorbent article or absorbent core respectively) is clamped nonwoven side upward onto the inspection table. A separatory funnel is positioned above the center of the test specimen so that the spout is directly above the insult point.

Measure 300 mL of Grade 2 water having conductivity at 25±1′C temperature of 0.1 Ms/m according to the EN ISO 3696:1995 using 500 mL glass beaker. Pour the water into the separatory funnel using the pouring glass funnel. The separatory funnel shall be controlled flow rate at 20 mL/sec. Pour the water through the separatory funnel at the center of test specimen, once the water first contact the specimen, simultaneously start a stopwatch. Allow the water to drain out from the separatory funnel and visually observe the waster being absorbed by the specimen. Once the top surface of the test specimen turn white, stop the stopwatch and record the “water pouring time” in seconds. Allow the test specimen to fully absorb the water for 30 seconds, monitored by a count-down timer. Prepare 30-40 pieces of filter paper (MN 615, OD 9 cm) and record its dry weight in grams (DW₁). After 30 seconds, place the filter paper on to the test specimen at the center and place 2.5 kgs circular weight with OD 8 cm (Picture 1) on top the filter paper. Wait for 30 seconds monitored by a timer, then take out the weight and the filter paper. Weigh the filter and record its wet weight in grams (WW₁).

Rewet (g)=WW ₁ (g)−DW ₁ (g)

The EDANA test methods are obtainable, for example, from the EDANA, Avenue Eugene Plasky 157, B-1030 Brussels, Belgium.

EXAMPLES Example 1

The process was performed in a concurrent spray drying plant with an integrated fluidized bed (27) as shown in FIG. 1. The reaction zone (5) had a height of 22 m and a diameter of 3.4 m. The internal fluidized bed (IFB) had a diameter of 3 m and a weir height of 0.25 m.

The drying gas was fed via a gas distributor (3) at the top of the spray dryer. The drying gas was partly recycled (drying gas loop) via a cyclone as dust separation unit (9) and a condenser column (12). The drying gas was nitrogen that comprises from 1% to 4% by volume of residual oxygen. Prior to the start of polymerization the drying gas loop was filled with nitrogen until the residual oxygen was below 4% by volume. The gas velocity of the drying gas in the reaction zone (5) was 0.81 m/s. The pressure inside the spray dryer was 4 mbar below ambient pressure.

The temperature of the gas leaving the reaction zone (5) was measured at three points around the circumference at the end of the cylindrical part of the spray dryer as shown in FIG. 3. Three single measurements (43) were used to calculate the average temperature (spray dryer outlet temperature). The drying gas loop was heated up and the dosage of monomer solution is started up. From this time the spray dryer outlet temperature was controlled to 119° C. by adjusting the gas inlet temperature via the heat exchanger (20). The gas inlet temperature was 167° C. and the steam content of the drying gas is shown in Tab. 1.

The product accumulated in the internal fluidized bed (27) until the weir height was reached. Conditioned internal fluidized bed gas having a temperature of 112° was fed to the internal fluidized bed (27) via line (25). The gas velocity of the internal fluidized bed gas in the internal fluidized bed (27) was 0.65 m/s. The residence time of the product was 150 min. The temperature of the water-absorbent polymer particles in the internal fluidized bed (27) was 80° C.

The spray dryer offgas was filtered in cyclone as dust separation unit (9) and sent to a condenser column (12) for quenching/cooling. Excess water was pumped out of the condenser column (12) by controlling the (constant) filling level inside the condenser column (12). The water inside the condenser column (12) was cooled by a heat exchanger (13) and pumped counter-current to the gas. The temperature and the steam content of the gas leaving the condenser column (12) are shown in Tab. 1. The water inside the condenser column (12) was set to an alkaline pH by dosing sodium hydroxide solution to wash out acrylic acid vapors.

The gas leaving the condenser column (12) was split to the drying gas inlet pipe (1) and the conditioned internal fluidized bed gas (25). The gas temperatures were controlled via heat exchangers (20) and (22). The hot drying gas was fed to the concurrent spray dryer via gas distributor (3). The gas distributor (3) consists of a set of plates providing a pressure drop of 2 to 4 mbar depending on the drying gas amount.

The product was discharged from the internal fluidized bed (27) via rotary valve (28) into sieve (29). The sieve (29) was used for sieving off overs/lumps having a particle diameter of more than 800 μm. The weight amounts of overs/lumps are summarized in Tab. 1.

The monomer solution was prepared by mixing first acrylic acid with 3-tuply ethoxylated glycerol triacrylate (internal crosslinker) and secondly with 37.3% by weight sodium acrylate solution. The temperature of the resulting monomer solution was controlled to 10° C. by using a heat exchanger and pumping in a loop. A filter unit having a mesh size of 250 μm was used in the loop after the pump. The initiators were metered into the monomer solution upstream of the dropletizer by means of static mixers (31) and (32) via lines (33) and (34) as shown in FIG. 1. Sodium peroxodisulfate solution having a temperature of 20° C. was added via line (33) and [2,2′-azobis[2-(2-imidazolin-2-yl)propane]dihydrochloride solution together with Brüggolite® FF7 and Blancolen® HP having a temperature of 10° C. was added via line (34). Each initiator was pumped in a loop and dosed via control valves to each dropletizer unit. A second filter unit having a mesh size of 140 μm was used after the static mixer (32). For dosing the monomer solution into the top of the spray dryer three dropletizer units were used as shown in FIG. 4.

A dropletizer unit consisted of an outer pipe (47) having an opening for the dropletizer cassette (49) as shown in FIG. 5. The dropletizer cassette (49) was connected with an inner pipe (48). The inner pipe (48) having a PTFE block (50) at the end as sealing can be pushed in and out of the outer pipe (47) during operation of the process for maintenance purposes.

The temperature of the dropletizer cassette (49) was controlled to 8° C. by water in flow channels (55) as shown in FIG. 8. The dropletizer cassette (49) had 256 bores having a diameter of 170 μm and a bore spacing of 15 mm. The dropletizer cassette (49) consisted of a flow channel (56) having essential no stagnant volume for homogeneous distribution of the premixed monomer and initiator solutions and one droplet plate (53). The droplet plate (53) had an angled configuration with an angle of 3°. The droplet plate (53) was made of stainless steel and had a length of 630 mm, a width of 128 mm and a thickness of 1 mm.

The feed to the spray dryer consisted of 9.56% by weight of acrylic acid, 33.73% by weight of sodium acrylate, 0.018% by weight of 3-tuply ethoxylated glycerol Triacrylate (purity approx. 85% by weight), 0.071% by weight of [2,2′-azobis[2-(2-imidazolin-2-yl)propane]dihydrochloride, 0.0028% by weight of Brüggolite® FF7 (Brüggemann Chemicals; Heilbronn; Germany), 0.036% by weight of Blancolene® HP (Brüggemann Chemicals; Heilbronn; Germany), 0.054% by weight of sodiumperoxodisulfate and water. The degree of neutralization was 73%. The feed per bore was 1.4 kg/h.

The resulting water-absorbent polymer particles were analyzed. The conditions and results are summarized in Tab. 1 to 3.

Example 2

The process was performed in a concurrent spray drying plant with an integrated fluidized bed (27) as shown in FIG. 1. The reaction zone (5) had a height of 22 m and a diameter of 3.4 m. The internal fluidized bed (IFB) had a diameter of 3 m and a weir height of 0.25 m.

The drying gas was fed via a gas distributor (3) at the top of the spray dryer. The drying gas was partly recycled (drying gas loop) via a cyclone as dust separation unit (9) and a condenser column (12). The drying gas was nitrogen that comprises from 1% to 4% by volume of residual oxygen. Prior to the start of polymerization the drying gas loop was filled with nitrogen until the residual oxygen was below 4% by volume. The gas velocity of the drying gas in the reaction zone (5) was 0.79 m/s. The pressure inside the spray dryer was 4 mbar below ambient pressure.

The temperature of the gas leaving the reaction zone (5) was measured at three points around the circumference at the end of the cylindrical part of the spray dryer as shown in FIG. 3. Three single measurements (43) were used to calculate the average temperature (spray dryer outlet temperature). The drying gas loop was heated up and the dosage of monomer solution is started up. From this time the spray dryer outlet temperature was controlled to 115° C. by adjusting the gas inlet temperature via the heat exchanger (20). The gas inlet temperature was 167° C. and the steam content of the drying gas is shown in Tab. 1.

The product accumulated in the internal fluidized bed (27) until the weir height was reached. Conditioned internal fluidized bed gas having a temperature of 108° was fed to the internal fluidized bed (27) via line (25). The gas velocity of the internal fluidized bed gas in the internal fluidized bed (27) was 0.65 m/s. The residence time of the product was 150 min. The temperature of the water-absorbent polymer particles in the internal fluidized bed (27) was 79° C.

The spray dryer offgas was filtered in cyclone as dust separation unit (9) and sent to a condenser column (12) for quenching/cooling. Excess water was pumped out of the condenser column (12) by controlling the (constant) filling level inside the condenser column (12). The water inside the condenser column (12) was cooled by a heat exchanger (13) and pumped counter-current to the gas. The temperature and the steam content of the gas leaving the condenser column (12) are shown in Tab. 1. The water inside the condenser column (12) was set to an alkaline pH by dosing sodium hydroxide solution to wash out acrylic acid vapors.

The gas leaving the condenser column (12) was split to the drying gas inlet pipe (1) and the conditioned internal fluidized bed gas (25). The gas temperatures were controlled via heat exchangers (20) and (22). The hot drying gas was fed to the concurrent spray dryer via gas distributor (3). The gas distributor (3) consists of a set of plates providing a pressure drop of 2 to 4 mbar depending on the drying gas amount.

The product was discharged from the internal fluidized bed (27) via rotary valve (28) into sieve (29). The sieve (29) was used for sieving off overs/lumps having a particle diameter of more than 800 μm. The weight amounts of overs/lumps are summarized in Tab. 1.

The monomer solution was prepared by mixing first acrylic acid with 3-tuply ethoxylated glycerol triacrylate (internal crosslinker) and secondly with 37.3% by weight sodium acrylate solution. The temperature of the resulting monomer solution was controlled to 10° C. by using a heat exchanger and pumping in a loop. A filter unit having a mesh size of 250 μm was used in the loop after the pump. The initiators were metered into the monomer solution upstream of the dropletizer by means of static mixers (31) and (32) via lines (33) and (34) as shown in FIG. 1. Sodium peroxodisulfate solution having a temperature of 20° C. was added via line (33) and [2,2′-azobis[2-(2-imidazolin-2-yl)propane]dihydrochloride solution together with Brüggolite® FF7 having a temperature of 10° C. was added via line (34). Each initiator was pumped in a loop and dosed via control valves to each dropletizer unit. A second filter unit having a mesh size of 140 μm was used after the static mixer (32). For dosing the monomer solution into the top of the spray dryer three dropletizer units were used as shown in FIG. 4.

A dropletizer unit consisted of an outer pipe (47) having an opening for the dropletizer cassette (49) as shown in FIG. 5. The dropletizer cassette (49) was connected with an inner pipe (48). The inner pipe (48) having a PTFE block (50) at the end as sealing can be pushed in and out of the outer pipe (47) during operation of the process for maintenance purposes.

The temperature of the dropletizer cassette (49) was controlled to 8° C. by water in flow channels (55) as shown in FIG. 8. The dropletizer cassette (49) had 256 bores having a diameter of 170 μm and a bore spacing of 15 mm. The dropletizer cassette (49) consisted of a flow channel (56) having essential no stagnant volume for homogeneous distribution of the premixed monomer and initiator solutions and one droplet plate (53). The droplet plate (53) had an angled configuration with an angle of 3°. The droplet plate (53) was made of stainless steel and had a length of 630 mm, a width of 128 mm and a thickness of 1 mm.

The feed to the spray dryer consisted of 9.56% by weight of acrylic acid, 33.73% by weight of sodium acrylate, 0.018% by weight of 3-tuply ethoxylated glycerol Triacrylate (purity approx. 85% by weight), 0.071% by weight of [2,2′-azobis[2-(2-imidazolin-2-yl)propane]dihydrochloride, 0.0028% by weight of Brüggolite® FF7 (Brüggemann Chemicals; Heilbronn; Germany), 0.071% by weight of sodiumperoxodisulfate and water. The degree of neutralization was 73%. The feed per bore was 1.4 kg/h.

The resulting water-absorbent polymer particles were analyzed. The conditions and results are summarized in Tab. 1 to 3.

Example 3

The process was performed in a concurrent spray drying plant with an integrated fluidized bed (27) as shown in FIG. 1. The reaction zone (5) had a height of 22 m and a diameter of 3.4 m. The internal fluidized bed (IFB) had a diameter of 3 m and a weir height of 0.25 m.

The drying gas was fed via a gas distributor (3) at the top of the spray dryer. The drying gas was partly recycled (drying gas loop) via a cyclone as dust separation unit (9) and a condenser column (12). The drying gas was nitrogen that comprises from 1% to 4% by volume of residual oxygen. Prior to the start of polymerization the drying gas loop was filled with nitrogen until the residual oxygen was below 4% by volume. The gas velocity of the drying gas in the reaction zone (5) was 0.79 m/s. The pressure inside the spray dryer was 4 mbar below ambient pressure.

The temperature of the gas leaving the reaction zone (5) was measured at three points around the circumference at the end of the cylindrical part of the spray dryer as shown in FIG. 3. Three single measurements (43) were used to calculate the average temperature (spray dryer outlet temperature). The drying gas loop was heated up and the dosage of monomer solution is started up. From this time the spray dryer outlet temperature was controlled to 115° C. by adjusting the gas inlet temperature via the heat exchanger (20). The gas inlet temperature was 167° C. and the steam content of the drying gas is shown in Tab. 1.

The product accumulated in the internal fluidized bed (27) until the weir height was reached. Conditioned internal fluidized bed gas having a temperature of 117° was fed to the internal fluidized bed (27) via line (25). The gas velocity of the internal fluidized bed gas in the internal fluidized bed (27) was 0.65 m/s. The residence time of the product was 150 min. The temperature of the water-absorbent polymer particles in the internal fluidized bed (27) was 78° C.

The spray dryer offgas was filtered in cyclone as dust separation unit (9) and sent to a condenser column (12) for quenching/cooling. Excess water was pumped out of the condenser column (12) by controlling the (constant) filling level inside the condenser column (12). The water inside the condenser column (12) was cooled by a heat exchanger (13) and pumped counter-current to the gas. The temperature and the steam content of the gas leaving the condenser column (12) are shown in Tab. 1. The water inside the condenser column (12) was set to an alkaline pH by dosing sodium hydroxide solution to wash out acrylic acid vapors.

The gas leaving the condenser column (12) was split to the drying gas inlet pipe (1) and the conditioned internal fluidized bed gas (25). The gas temperatures were controlled via heat exchangers (20) and (22). The hot drying gas was fed to the concurrent spray dryer via gas distributor (3). The gas distributor (3) consists of a set of plates providing a pressure drop of 2 to 4 mbar depending on the drying gas amount.

The product was discharged from the internal fluidized bed (27) via rotary valve (28) into sieve (29). The sieve (29) was used for sieving off overs/lumps having a particle diameter of more than 800 μm. The weight amounts of overs/lumps are summarized in Tab. 1.

The monomer solution was prepared by mixing first acrylic acid with 3-tuply ethoxylated glycerol triacrylate (internal crosslinker) and secondly with 37.3% by weight sodium acrylate solution. The temperature of the resulting monomer solution was controlled to 10° C. by using a heat exchanger and pumping in a loop. A filter unit having a mesh size of 250 μm was used in the loop after the pump. The initiators were metered into the monomer solution upstream of the dropletizer by means of static mixers (31) and (32) via lines (33) and (34) as shown in FIG. 1. Sodium peroxodisulfate solution having a temperature of 20° C. was added via line (33) and [2,2′-azobis[2-(2-imidazolin-2-yl)propane]dihydrochloride solution together with Brüggolite® FF7 and Blancolen® HP having a temperature of 10° C. was added via line (34). Each initiator was pumped in a loop and dosed via control valves to each dropletizer unit. A second filter unit having a mesh size of 140 μm was used after the static mixer (32). For dosing the monomer solution into the top of the spray dryer three dropletizer units were used as shown in FIG. 4.

A dropletizer unit consisted of an outer pipe (47) having an opening for the dropletizer cassette (49) as shown in FIG. 5. The dropletizer cassette (49) was connected with an inner pipe (48). The inner pipe (48) having a PTFE block (50) at the end as sealing can be pushed in and out of the outer pipe (47) during operation of the process for maintenance purposes.

The temperature of the dropletizer cassette (49) was controlled to 8° C. by water in flow channels (55) as shown in FIG. 8. The dropletizer cassette (49) had 256 bores having a diameter of 170 μm and a bore spacing of 15 mm. The dropletizer cassette (49) consisted of a flow channel (56) having essential no stagnant volume for homogeneous distribution of the premixed monomer and initiator solutions and one droplet plate (53). The droplet plate (53) had an angled configuration with an angle of 3°. The droplet plate (53) was made of stainless steel and had a length of 630 mm, a width of 128 mm and a thickness of 1 mm.

The feed to the spray dryer consisted of 9.56% by weight of acrylic acid, 33.73% by weight of sodium acrylate, 0.013% by weight of 3-tuply ethoxylated glycerol Triacrylate (purity approx. 85% by weight), 0.071% by weight of [2,2′-azobis[2-(2-imidazolin-2-yl)propane]dihydrochloride, 0.0028% by weight of Brüggolite® FF7 (Brüggemann Chemicals; Heilbronn; Germany), 0.054% by weight of Blancolene® HP (Brüggemann Chemicals; Heilbronn; Germany) 0.099% by weight of sodiumperoxodisulfate and water. The degree of neutralization was 73%. The feed per bore was 1.4 kg/h.

The resulting water-absorbent polymer particles were analyzed. The conditions and results are summarized in Tab. 1 to 3.

TABLE 1 Process conditions of the polymerization for examples 1 to 7 Steam Steam T T T Content Content gas gas gas T T T CC GD inlet outlet IFB IFB CC GDU Example kg/kg kg/kg ° C. ° C. ° C. ° C. ° C. ° C. 1 0.1100 0.0651 167 119 112 80 54 45 2 115 108 79 3 115 107 77 Steam Content CC: steam content of the gas leaving the condenser column (12) Steam Content GD: steam content of the gas prior to the gas distributor (3) T gas inlet: temperature of the gas prior to the gas distributor (3) T gas outlet: temperature of the gas leaving the reaction zone (5) T gas IFB temperature of the gas entering the internal fluidized bed (27) via line (25) T IFB: temperature of the water-absorbent polymer particles in the fluidized bed (27) T CC: temperature of the gas leaving the condenser column (12) T GDU: temperature of the gas leaving the gas drying unit (37)

TABLE 2 Properties of the water-absorbent polymer particles (base polymer) Bulk Density CRC AUL Residual Monomers Extractables Moisture Example g/cm³ g/g g/g Ppm wt. % wt. % L a b 1 65.0 60.4 7.6 6820 15.9 7.6 93.4 2.1 2.4 2 70.3 50.2 7.9 5150 5.8 8.0 93.0 2.3 2.1 3 69.3 61.8 7.8 5250 11.8 8.2 94.2 2.2 3.0

TABLE 3 Particles Size Distribution (PSD) of the water-absorbent polymer particles (base polymer), measured by sieve fraction analysis 0-100 μm 100-200 μm 200-250 μm 250-300 μm 300-400 μm 400-500 μm 500-600 μm 600-850 μm 850-1000 μm >1000 μm Example wt % wt % wt % wt % wt % wt % wt % wt % wt % wt % 1 0.0 0.7 4.2 7.5 32.7 33.4 11.9 9.0 0.6 0.0 2 0.6 4.2 7.5 11.3 40.3 26.6 6.4 2.7 0.3 0.1 3 0.4 1.9 5.2 8.2 32.2 32.7 10.1 8.3 0.9 0.1

Examples 4 and 5 General Description

In a Schugi Flexomix® (model Flexomix 160, manufactured by Hosokawa Micron B.V., Doetinchem, the Netherlands) with a speed of 2000 rpm, the base polymer was coated with a surface-postcrosslinker solution by using 2 or 3 round spray nozzle systems (model Gravity-Fed Spray Set-ups, External Mix Typ SU4, Fluid Cap 60100 and Air Cap SS-120, manufactured by Spraying Systems Co, Wheaton, Ill., USA) and then filled via base polymer feed (70) and dried in a thermal dryer (65) (model NPD 5W-18, manufactured by GMF Gouda, Waddinxveen, the Netherlands) with a speed of the shaft (76) of 6 rpm. The thermal dryer (65) has two paddles with a shaft offset of 90° (80) and a fixed discharge zone (71) with two flexible weir plates (73). Each weir has a weir opening with a minimal weir height at 50% (75) and a maximal weir opening at 100% (74) as shown in FIG. 15.

The inclination angle α (78) between the floor plate and the thermal dryer was approx. 3°. The weir height of the thermal dryer was between 50 to 100%, corresponding to a residence time of approx. 40 to 150 min, by a product density of approx. 700 to 750 kg/m³. The product temperature in the thermal dryer was in a range of 120 to 165° C. After drying, the surface-postcrosslinked polymer was transported over discharge cone (77) in a cooler (model NPD 5W-18, manufactured by GMF Gouda, Waddinxveen, the Netherlands), to cool down the surface postcrosslinked polymer to approx. 60° C. with a speed of 11 rpm and a weir height of 145 mm. After cooling, the material was sieved with a minimum cut size of 150 μm and a maximum cut size of 710 μm.

Example 4

Ethylene carbonate, water, Plantacare® UP 818 (BASF SE, Ludwigshafen, Germany) and aqueous aluminum lactate (22% by weight) were premixed and used as surface-postcrosslinker solution as summarized in Tab. 5. As aluminum lactate, Lothragon® Al 220 (manufactured by Dr. Paul Lohmann GmbH, Emmerthal, Germany) was used.

5.0 wt % of a 0.05% aqueous solution of Plantacare® UP 818, having a temperature of approx. 25° C., was additionally added into the cooler using two nozzles in the first third of the cooler. The nozzles were placed below the product bed.

The resulting water-absorbent polymer particles were analyzed. The trial conditions and results are summarized in Tab. 4 to 7.

Example 5

Ethylene carbonate, water, Span® 20 (Croda, Nettetal, Germany)), aqueous aluminum lactate (22% by weight) were premixed and used as surface-postcrosslinker solution as summarized in Tab. 5. As aluminum lactate, Lothragon® Al 220 (manufactured by Dr. Paul Lohmann GmbH, Emmerthal, Germany) was used.

4.0 wt % of a 0.125% aqueous solution of Span®20 solution (Croda, Nettetal, Germany) and 4.4 wt % of a 5.7% aqueous solution of aluminum lactate solution were additionally added into the cooler using two nozzles in the first third of the cooler. Both solution having a temperature of approx. 25° C. The nozzles were placed below the product bed.

The resulting water-absorbent polymer particles were analyzed. The trial conditions and results are summarized in Tab. 4 to 8.

TABLE 4 Process conditions of the thermal dryer for the surface postcrosslinking (SXL) Product Temp. Steam Steam Set Pressure Pressure Heater Heater Heater Heater Heater Heater Through- Heater Example Value Wave Jacket T1 T2 T3 T4 T5 T6 put Weir No. of Pos. of Unit ° C. Bar Bar ° C. ° C. ° C. ° C. ° C. ° C. kg/h % Nozzles Nozzles 4 145 5.2 4.8 96 98 116 127 135 145 470 80 3 90/180/270° 5 145 4.7 4.6 95 99 118 129 139 145 470 80 3 90/180/270°

TABLE 5 Surface-postcrosslinker formulation of the thermal treatment in the heater and remoistening in the cooler Cooler SXL 0.05 wt % Plantacare ® 0.125 wt % 5.7 wt % aq. solution of Al-lactate UP 818 aq. solution of aq. solution of Plantacare ® UP 818 Base EC Water (dry) (dry) Span ®20 aluminum lactate (dry) Example polymer bop % bop % bop % bop ppm bop % bop % bop % 4 Example 2 2.0 5.0 0.1 25 5.0 5 Example 3 2.0 5.0 0.1 4.0 4.4 EC: Ethylene carbonate; bop: based on polymer

TABLE 6 Physical properties of the polymer particles after surface-postcrosslinking CRC AUL AUHL Moisture Residual Monomers Extractables Bulk Density Example g/g g/g g/g % ppm % g/100 ml 4 44.4 34.9 25.1 4.7 369 4 85 5 48.4 35.2 15.6 6.2 531 7 86

TABLE 7 Particle size distribution of the polymer particles after surface-postcrosslinking - Sieve fractions <106 μm >106 μm >200 μm >250 μm >300 μm >400 μm >500 μm >600 μm >710 μm Example % % % % % % % % % 4 0.0 0.3 2.2 20.9 58.8 16.7 1.0 0.1 0.0 5 0.1 1.1 6.3 12.4 46.9 27.2 4.3 1.6 0.1

TABLE 8 Color stability of the polymer particles after surface-postcrosslinking (Accelerated Aging Test) 0 d 7 d 14 d 21 d Example L A B L A b L a b L a b 5 93.6 −1.7 10.9 83.8 −1.0 10.6 83.9 −0.7 11.1 82.9 −0.5 12.1

Example 6 Preparation of Absorbent Paper/Absorbent Core:

Hot melt glue (2.0 gsm, construction hot melt adhesive by Bostik) is sprayed on to tissue bottom layer (45 gsm, condensed tissue made by Fujian Qiao Dong-Paper Co., Ltd.), SAP (bottom layer) is then applied on to the tissue at 130 gsm loading using roller feeder (commercial available SAP feeder roller type). High loft nonwoven material (50 gsm, air-through bond nonwoven of polyester by Fujian Qiao Dong-Paper Co., Ltd.) is fed into the lamination equipment, hot melt glue is sprayed on to the nonwoven (0.5 gsm, construction hot melt adhesive by Bostik). The nonwoven containing hot melt glue is then laminated with the tissue layer hot melt glue and SAP. This gives the bottom layer of the absorbent paper.

Another layer is prepared by spraying hot melt glue (2.0 gsm) on to another tissue sheet (top layer, condensed tissue made by Fujian Qiao Dong-Paper Co., Ltd.), and then another type of SAP (130 gsm) is applied on to the tissue layer. This gives second layer of absorbent paper.

The first layer and second layer are then laminated together using hot melt glue (0.5 gsm, construction hot melt adhesive by Bostik) by passing through a compression rolls (commercial available metal compression rollers). This results in a complete absorbent paper.

Absorbent paper consists of two layers of superabsorbent polymers (SAP) one of which laid on top side (91) and another laid on the bottom of the sheet (92). Both top and bottom SAP layers contain 130 grams per square meter (g/m²). Both layers are glued (93) with 0.5 g/m² hot melt adhesive on 50 g/m² air-thru-bond nonwoven material (94) and are then sandwiched with two layers of 45 g/m² condensed tissue layers on the top (95) and bottom (96) using hot-melt glue applied to the surface at 2.0 g/m². Total hot-melt glue used is 2.5 g/m² for both top and bottom layers. (the numbers refer to FIG. 17)

The lamination sheet (hereunder called specimen) is cut to give 95 mm width and 400 mm length.

Cut to dimension absorbent paper is inserted into a pre-made tape diaper sachet having 2-layered embossed nonwoven topsheet with g/m2 (Daddy Baby diapers size-L, tape type, made by Fuzhou Angel Commodity Co., Ltd). The specimen has no acquisition layer. Both spunbond nonwoven leg cluff have 35 mm height and two elastic strands. The distance between the tack-down leg cluff and the absorbency core for both sides is 10 mm width. The dimension of the absorbency core is the same dimension of the absorbent paper used.

Example 7 Preparation of Diaper Samples.

A commercial tape diaper having 2-layered embossed nonwoven topsheet with 52 gsm (Daddy Baby diapers size-L, tape type, made by Fuzhou Angel Commodity Co., Ltd). The diaper sample is cut from the backsheet in the middle. The original absorbent core is carefully removed. The diaper sample has no acquisition layer. Both spunbond nonwoven leg cuffs (left and right) have 35 mm height and two elastic strands. The distance between the tack-down leg cuff and the absorbency core for both sides is 10 mm width. Other materials remain the same giving an empty like diaper sachet.

The Lab laminated absorbent paper/absorbent core is cut using scissor to give a dimension of 400 mm length and 95 mm width. This sheet of absorbent paper is inserted and placed into diaper sachet replacing the original absorbent core. The diaper sample is then carefully sealed by adhesive tape to form diaper sample for Lab testing.

Example 8 Different Absorbent Papers are Produced

-   1 Top layer (91) 130 gsm Example 2     -   Bottom layer (92) 130 gsm Aquakeep SA60SX-II by Sumitomo Seika         Chemicals Co., Ltd., Japan -   2 Top layer (91) 130 gsm Example 4     -   Bottom layer (92) 130 gsm Aquakeep SA60SX-II by Sumitomo Seika         Chemicals Co., Ltd., Japan -   3 Top layer (91) 130 gsm Sanwett IM930, San-Dia Polymers, Ltd.     -   Bottom layer (92) 130 gsm Aquakeep SA60SX-II by Sumitomo Seika         Chemicals Co., Ltd., Japan

Example 9

For the absorbent papers according to example 8 the Water Pouring Time and Rewet is determined. The results are summarized in Tab. 9

TABLE 9 Water Pouring Time and Rewet Test results Water pouring time Rewet Top layer (91) Bottom layer (92) (sec) (g) 1 Example 2 Aquakeep SA60SX-II 38 7.7 2 Example 4 Aquakeep SA60SX-II 28 0.4 3 Sanwett IM 930 Aquakeep SA60SX-II 23 0.7

The results show that the absorbent paper with surface-postcross-linked Example 4 in the top layer (91) and Aquakeep SA60SX-II on the bottom layer showed the lowest rewet than the other absorbent paper tested.

Example 10

For the absorbent papers as described in Example 8 the Quick dryness is also measured. The results are summarized in Tab. 10.

TABLE 10 Dryness Test results Quick Dryness Top layer (91) Bottom layer (92) (g) 1 Example 2 Aquakeep SA60SX-II 7.7 2 Example 4 Aquakeep SA60SX-II 1.8 3 Sanwett IM 930 Aquakeep SA60SX-II 3.4

Example 11

For the absorbent papers as described in Example 8 Strike-thru time and Rewet (Chinese Standard) are determined.

The results are summarized in Tab. 11.

TABLE 11 Strike-thru time and Rewet Test results Strike-thru time (sec) Rewet Top layer (91) Bottom layer (92) 1st 2nd (g) 1 Example 2 Aquakeep SA60SX-II 13 13 14.2 2 Example 4 Aquakeep SA60SX-II 8 8 4.1 3 Sanwett IM930 Aquakeep SA60SX-II 9 8 7.0

Absorbent paper with Example 4 in the top layer (91) and Aquakeep SA60SX-II in the bottom layer (92) show significant lower rewet than the other tested absorbent papers.

Example 12

The properties of the water-absorbent particles of example 8 are listed in Tab. 12.

TABLE 12 Properties of the water-absorbent polymers AAP 0.3 CRC + Water-absorbent polymer particle CRC (g/g) psi (g/g) AAP 1 Aquakeep SA60-SX-II 35.5 27.6 63.1 2 Example 2 50.2 7.9 58.1 3 Sanwett IM930 30.1 24.6 54.7 4 Example 4 44.4 34.9 79.3 

1. A fluid-absorbent core (80), comprising at least two layers, an upper layer (91) and a lower layer (92), each layer comprising from 0 to 10% by weight fibrous material and from 90 to 100% by weight water-absorbent polymer particles, based on the sum of water-absorbent polymer particles and fibrous material; wherein the water absorbent polymer particles within the upper layer (91) have a sphericity of at least 0.89 and at least one of a CRC of at least 34 g/g and a sum of a CRC and AUL (21 g/cm², EDANA 442.2-02) of the water absorbent polymer particles is at least 65 g/g.
 2. (canceled)
 3. The fluid-absorbent article according to claim 1, wherein the AUL (21 g cm⁻², EDANA 442.2-02) for the water absorbent polymer particles of the upper layer (91) is at least 30 g/g.
 4. The fluid-absorbent article according to claim 1, wherein the upper layer (91) comprises 100% by weight of water-absorbent particles.
 5. The fluid-absorbent article according to claim 1, wherein the lower layer (92) comprises 100% by weight of water-absorbent particles.
 6. The fluid-absorbent article according to claim 1, wherein a nonwoven material (94) is sandwiched between the upper layer (91) and the lower layer (92).
 7. The fluid-absorbent article according to claim 6, wherein the layers (91, 92) are glued on the nonwoven material (94) by an adhesive, ultrasonic bonding, and/or heat bonding.
 8. The fluid-absorbent core according to claim 1, wherein an upper tissue layer (95) and/or an lower tissue layer (96) is attached to the surface of the upper layer (91) and the lower layer (92) respectively.
 9. The fluid-absorbent core according to claim 8, wherein the attachment is performed by an adhesive, ultrasonic bonding, and/or heat bonding.
 10. The fluid-absorbent article according to claim 1, wherein the fluid absorbent core (80) comprises not more than 10% by weight of adhesive.
 11. The fluid-absorbent core according to claim 1, wherein the water absorbent polymer particles in each layer (91, 92) are different.
 12. Absorbent article, comprising (A) an upper liquid-pervious sheet (89), (B) a lower liquid-impervious sheet (83), (C) a fluid-absorbent core (80) according to claim 1, (D) an optional acquisition-distribution layer (D) between (89) and (80), (F) other optional components.
 13. The absorbent article according to claim 12, wherein the upper tissue layer (95) and/or the lower tissue layer (96) correspond to the upper liquid-pervious sheet (89) and/or lower liquid-impervious sheet (83), respectively. 